TWI300006B - Coagulating and separating apparatus - Google Patents

Coagulating and separating apparatus Download PDF

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Publication number
TWI300006B
TWI300006B TW094134072A TW94134072A TWI300006B TW I300006 B TWI300006 B TW I300006B TW 094134072 A TW094134072 A TW 094134072A TW 94134072 A TW94134072 A TW 94134072A TW I300006 B TWI300006 B TW I300006B
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Taiwan
Prior art keywords
separation
coagulation
doc
water
tank
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TW094134072A
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Chinese (zh)
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TW200621345A (en
Inventor
Yasuo Yamada
Shunsoku Kyosai
Norimitsu Morikawa
Minoru Sato
Koji Nishihara
Shinichi Nagamatsu
Masami Oura
Ryuma Sakurai
Hiroko Mase
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Nishihara Environment Tech Inc
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Publication of TW200621345A publication Critical patent/TW200621345A/en
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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/01—Separation of suspended solid particles from liquids by sedimentation using flocculating agents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0012—Settling tanks making use of filters, e.g. by floating layers of particulate material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
    • B01D21/0042—Baffles or guide plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2427—The feed or discharge opening located at a distant position from the side walls
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2444—Discharge mechanisms for the classified liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/245—Discharge mechanisms for the sediments
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2488—Feed or discharge mechanisms for settling tanks bringing about a partial recirculation of the liquid, e.g. for introducing chemical aids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/28—Mechanical auxiliary equipment for acceleration of sedimentation, e.g. by vibrators or the like
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/28—Mechanical auxiliary equipment for acceleration of sedimentation, e.g. by vibrators or the like
    • B01D21/286—Means for gentle agitation for enhancing flocculation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/30—Control equipment
    • B01D21/32—Density control of clear liquid or sediment, e.g. optical control ; Control of physical properties
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5281—Installations for water purification using chemical agents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/26—Separation of sediment aided by centrifugal force or centripetal force
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00—General aspects of water treatment
    • C02F2301/04—Flow arrangements
    • C02F2301/046—Recirculation with an external loop
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/24—Separation of coarse particles, e.g. by using sieves or screens
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00—Use of specific compounds during water treatment
    • C02F2305/12—Inert solids used as ballast for improving sedimentation

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)

Description

1300006 九、發明說明： 【發明所屬之技術領域】 本發明係關於一種凝聚及分離裝置，在該凝聚及分離裝 置中將包含諸如膠狀物質或微粒等懸浮物質之起始水（例 如，生水、流入水）與凝聚劑混合，使懸浮物質凝聚，以 便形成絮凝物（凝聚汙物），並使該絮凝物自該起始水經受 固體-液體分離，以便可持續獲得清潔水。 【先前技術】 得統 浮物質等的擬處理水經由一生水注入管流入該凝聚反應 罐。自一凝聚劑供應構件向流入該凝聚反應罐中的擬處理 水添加凝聚劑。自-添加劑供應構件向流人該凝聚反應罐 中的擬處理水供應諸如沙子等不溶性添加劑。此外，該凝 聚及分離裝置具有一混合物抽吸構件、—固體_液體分離 罐、-幫浦、-回流管及-添加劑回收器件。該混合物抽 吸構件自該凝聚反應罐抽吸出—混合物。該固體_液體分 =對來自該凝聚反應罐之流出水予以固體-液體分離。 =*構造成一分離物體抽吸構件，用以自該固體·液體 旧括# .、.、 亥添加劑回收器件分離經由該 :官自該幫浦返回的分離物體中所含添加劑並回收該 寻添加劑。該添加劑回收器件進一牛 到該凝聚反應罐中並向系統外部放斤口收添加』返回 而言，參見專利文獻… 排放刀離出的汙物（舉例 專利文獻1:日本㈣未審核公開案第2003_326110號 105052.doc 1300006 (第2頁，右列第14至26行，圖1) 傳統凝聚及分離裝置於向凝聚反應罐中添加凝聚劑形 成絮凝物後在固體-液體分離罐中藉助重力使絮凝物自擬 處理水分離。因此，會存在這樣一個問題，即整個設施場 所佔地必須大，此乃因額外需要固體-液體分離罐並且該 固體-液體罐之大小至少與該凝聚反應罐相等。此外，由 於絮凝物係藉助重力自擬處理水分離，故處理之實施速率 不能超出絮凝物之沉降速率。因此，處理效率較低。 • 【發明内容】 本發明致力於解決上述問題。本發明之目的在於提供一 種凝聚及分離裝置，該裝置能降低設施場所佔地並更快及 更穩定地實施固體-液體分離，換言之，其可減少設施場 所佔地，縮短處理時間，並更穩定地實施處理。 本發明凝聚及分離裝置之特徵在於包含一凝聚及分離</ RTI> </ RTI> </ RTI> </ RTI> </ RTI> </ RTI> </ RTI> </ RTI> </ RTI> </ RTI> </ RTI> </ RTI> </ RTI> </ RTI> < Desc/Clms Page number> The influent water is mixed with the coagulant to agglomerate the suspended matter to form a floc (condensed dirt), and the floc is subjected to solid-liquid separation from the starting water so that clean water can be continuously obtained. [Prior Art] The water to be treated, such as a floating substance, flows into the coagulation reaction tank through a raw water injection pipe. A coagulant is added from a coagulant supply member to the water to be treated flowing into the coagulation reaction tank. The self-additive supply member supplies an insoluble additive such as sand to the water to be treated in the coagulation reaction tank. Further, the coagulation and separation device has a mixture suction member, a solid_liquid separation tank, a pump, a reflux tube, and an additive recovery device. The mixture suction member draws a mixture from the coagulation reaction tank. The solids_liquid fraction = solid-liquid separation of the effluent water from the coacervation tank. =* is configured as a separate object suction member for separating the additive contained in the separated object returned from the pump and recovering the additive from the solid/liquid additive #.,. . The additive recovery device is fed into the coagulation reaction tank and added to the outside of the system. For the return, see the patent document... The dirt that is discharged from the discharge knife (Example Patent Document 1: Japan (4) Unaudited Publication No. 2003_326110 No. 105052.doc 1300006 (Page 2, right column, lines 14 to 26, Fig. 1) Conventional coagulation and separation device is formed by adding gravity to a coagulating reaction tank to form flocs and then by gravity in a solid-liquid separation tank. The floc is self-treated to treat water separation. Therefore, there is a problem that the entire facility site must occupy a large area because an additional solid-liquid separation tank is required and the solid-liquid tank is at least equal in size to the condensation reaction tank. In addition, since the floc is self-treated by gravity to treat the water separation, the rate of implementation of the treatment cannot exceed the sedimentation rate of the floc. Therefore, the treatment efficiency is low. The present invention is directed to solving the above problems. The purpose of the invention is to provide a coagulation and separation device which can reduce the footprint of the facility and implement the solid-liquid faster and more stably. Body separation, in other words, it can reduce the footprint of the facility, shorten the processing time, and perform the treatment more stably. The condensation and separation device of the present invention is characterized by including a condensation and separation.

流入該凝聚及分離罐中。該水流發生器在該凝聚及分離罐 中產生循環流或渦流。該汙物轉移管轉移凝聚的汙物。Flow into the coagulation and separation tank. The water flow generator produces a circulating or vortex in the coagulation and separation tank. The dirt transfer tube transfers the condensed dirt.

輪之攪拌器。提供一 /主入官’以將與凝聚劑混合之生水注 發生益構造成一具有一軸流式攪拌葉 汗物收集箱以增厚凝聚的汙物。提供 105052.doc 1300006 一管路混合物以混合凝聚劑與生水。於該凝聚及分離罐中 提供水品質篁測儀器。另外，向所注入之處理後的水提 供一集水池。 本發明利用凝聚劑形成絮凝物並利用水流發生器產生 渦机口此，本發明允許絮凝物於1個凝聚及分離罐中持 貝刀離換5之’由於凝聚及分離可同時實施，故形成絮 凝物及固體-液體分離可於同一凝聚及分離罐中進行。另 外’由於S1體·液體分離可高效且穩线實施，故不需要 所佔地大等的傳統固體_液體分離罐。整個裝置小 型化。建造費用降低。 若提供導流管，則可設定一約2至3分鐘之停留時間，並 可維持8G%或以上之88移除率。若始終量測絮凝物在凝聚 及罐中之狀況或處理後的水之狀況，則可總能維持一科定 的介面及適宜量的m此外，可持續而穩定地實施處 若與凝聚劑混合之擬處理水流入該凝聚及分離罐並藉 由該水流發生器㈣’則可於該凝聚及分離罐中產生渦 流。另外，若該導流管佈置成環繞該水流發生構件且若進 步佈置一水平導流板及一垂直、☆ ^ ^ ^ ^ ^ ^ ^ 直导/爪板，則可平穩地形成 此外，若佈置-多孔元件，則可更敎地產生水平 ;(例：向心流)及渦流(例如下降流)來控制向上之流動速 率。因此，可穩定處理之效率。 二僅tr專統凝聚及沉降處理使用的凝聚劑，而且注 入具“比重之材料並進—步添加凝聚助劑，則可形成較 105052.doc 1300006 先刚絮凝物大的絮凝物。在此一情況下，由於絮凝物之質 量增大，故可提高處理速率，縮短停留時間，高效而穩定 地實施處理。並且，若將擬於凝聚反應中起作用之具有高 比重之材料自汙物收集箱抽吸出來，轉移至分離器，自汙 物分離並持續供應至擬處理水，則可重新利用該具有高比 重之材料。可降低維護及控制成本。 【實施方式】 第一實施例Wheel agitator. A primary/administrator is provided to construct a raw water injection mixing agent with a coagulant to form an axial flow agitating leaf sweat collection bin to thicken the agglomerated dirt. A 105052.doc 1300006 line mixture is provided to mix the coagulant with raw water. A water quality measuring instrument is provided in the coagulation and separation tank. In addition, a pool of treated water is supplied to the treated water. The invention utilizes a flocculating agent to form a floc and uses a water flow generator to generate a vortex machine port. The present invention allows the floc to be held in a coagulation and separation tank by a knife. The coagulation and separation can be simultaneously performed, so that Flocs and solid-liquid separations can be carried out in the same coacervate and separation tank. Further, since the S1 body and the liquid separation can be carried out efficiently and stably, a conventional solid-liquid separation tank having a large area is not required. The entire device is miniaturized. Construction costs are reduced. If a draft tube is provided, a residence time of about 2 to 3 minutes can be set and an 88 removal rate of 8 G% or more can be maintained. If the condition of the floc in the agglomerate and the tank or the condition of the treated water is always measured, it is always possible to maintain a certain interface and an appropriate amount of m. In addition, it can be continuously and stably mixed with the coagulant. The treated water flows into the coagulation and separation tank and the vortex is generated in the coagulation and separation tank by the water flow generator (4). In addition, if the draft tube is arranged to surround the water flow generating member and if a horizontal baffle and a vertical, ☆ ^ ^ ^ ^ ^ ^ ^ straight guide/claw plate are arranged, the smoothing can be formed smoothly, if - Porous elements, which can produce levels more ambiguously; (for example: centripetal flow) and eddy currents (such as downflow) to control the upward flow rate. Therefore, the efficiency of the processing can be stabilized. 2. Only the coagulant used in the special condensation and sedimentation treatment of tr, and the injection of the material with the specific gravity and the addition of the coagulation aid, can form a floc larger than the 105052.doc 1300006 first floc. In this case In the following, since the mass of the floc is increased, the treatment rate can be increased, the residence time can be shortened, and the treatment can be carried out efficiently and stably. Moreover, if a material having a high specific gravity which is intended to function in the aggregation reaction is collected from the dirt collection box, After being sucked out, transferred to the separator, separated from the dirt and continuously supplied to the water to be treated, the material having a high specific gravity can be reused, and maintenance and control costs can be reduced.

圖1係方塊圖’其顯示本發明凝聚及分離裝置之第一 實施例。該凝聚及分離裝置具有一凝聚及分離罐丨，其用 於凝聚生水中的懸浮物質等以實施固體_液體分離。生水 經由一生水注入管3、一用於添加具有高比重之材料之構 =4及一生水注入管5自一混合罐2流入凝聚及分離罐卜混 s罐2 /、有生水流入口 2a及一凝聚劑注入口 生水於 生水流入°2a流人。提供凝聚劑注人口 2b係用於注入凝聚 劑6。混合罐2以某一停留時間於生水中維持滿流。混合罐 2使生水中之懸浮物質與凝聚劑6反應形成絮凝物。在用於 添加具有高比重之材料之構造4中，安裝一篩網7以去除生 水中之雜質。於用於添加具有高比重之材料之構造4上方 安裝一分離器8。具有高比重之材料9自分離器8添加至用 於添加具有高比重之材料之構造4中。生水注入管5於用於 ^加具有高比重之材料之構造4之下游提供。凝聚助劑ι〇 自-凝聚助劑注入口 10a注入生水注入管5 劑1 〇使具有高比重之材料9盥絮、疑物奋八姪雄 破來助 〜 U物充分接觸而形成較重 ’、佚，攸而產生較佳的固體-液體分離。 105052.doc 1300006 在混合罐2中，較佳提供一攪拌器來形成湍流，其未於 該圖中示出。生水注入管5之生水注入口 5a之位置被設置 為可容易地達成漂浮於凝聚及分離罐1中之湍流之上。篩 網7之位置並無限制，只要其位於凝聚及分離罐1之上游。 然而’為防止分離器8閉合，篩網7較佳提供於添加具有高 比重之材料9處的上游。即使其安裝於混合罐2之前，亦不 會出現問題。不言而喻，若生水中不含雜質，則無需安裝 篩網7。設置添加凝聚助劑10及具有高比重之材料9之位 置，以使具有高比重之材料9與凝聚助劑1 〇將同時反應以 促進絮凝物之形成。儘管添加具有高比重之材料9之位置 可位於旋聚及分離罐1之上游侧，但具有高比重之材料9 較佳於凝聚及分離罐1與混合罐2之間添加。添加凝聚助劑 10之位置可係在混合液體流入凝聚及分離罐1中之前。添 加凝聚助劑10之位置亦可係於靠近凝聚及分離罐1中生水 注入口 5a注入混合液體後凝聚助劑1〇直接充分混合處。 於滅聚及分離罐1之中部提供一水流發生器1 1，用於擾 拌流動的混合液體（即生水與凝聚劑6混合的液體），即擬 處理水，以產生水流。於凝聚及分離罐丨之上部提供一集 水池12，用於收集藉由實施固體_液體分離獲得的處理後 的水。處理後的水經由處理後的水之出口丨2a自集水池J2 注入系統外部。於凝聚及分離罐i之下部，提供一汙物排 放口 13 ’用於排放自擬處理水分離出的汙物。於凝聚及分 離罐1之外部下側提供一汙物收集箱14，用於收集來自汙 物排放口 1 3之汗物。汗物收集箱14中之汙物經由一汙物轉 105052.doc -11 - 1300006 移官15轉移至分離器8。自汙物收集箱14之一側於汙物轉 移官15上依序佈置一打開及閉合閥丨6及一轉移幫浦丨7。凝 聚及分離罐1A具有一品質量測儀器1 8，用於量測汙物介面 κ處水之品質。水品質量測儀器18與打開及閉合閥16相 連，以便基於來自水品質量測儀器18之信號驅動打開及閉 合閥16。 凝聚及分離罐i較佳構造成一圓柱體形狀。然而，考慮 到空間之有效利用及建造成本，凝聚及分離罐1可構造成 立方體（直角平行六面體）。凝聚及分離罐丨可係一多面體 而非一平面形狀。在此一情況下，其較佳具有一為均勻且 對稱的多面體之形狀。若於容量相同的情況下對高與矮加 以比較’則即使在容量相同的情況下後者亦不適於產生渦 流。因此，凝聚及分離罐1之高度較佳大於水平方向之長 度（直徑或寬度）。換言之，若凝聚及分離罐1之形狀為圓 柱體’則高與直徑之比率設定為1或更大。若其具有一直 角平行/、面體形狀’則高度與水平方向長度之比率設定為 1或更大。然而，即使凝聚及分離罐丨在水平方向上較長， 於凝聚及分離罐1中佈置一隔離物亦可產生平穩的渴流。 在類似情況下，若凝聚及分離罐1上部之直徑較其下部之 直徑大，則與下部分相比可放慢凝聚及分離罐1上部渦流 之上升速率。因此可有效地產生汙物介面K。 凝聚劑6使用具有大量離子電荷的鐵系列及鋁系列無機 凝聚劑。聚氯化鋁、硫酸鋁、氯化鐵、硫酸鐵等可作為此 類無機凝聚劑。然後，凝聚劑6之種類並無限制，尸要可 105052.doc -12- !3〇0〇〇6 充分地形成絮凝物。BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a block diagram showing a first embodiment of the agglomeration and separation apparatus of the present invention. The coagulation and separation device has a coagulation and separation tank which is used to condense suspended matter in raw water to perform solid-liquid separation. The raw water flows through the raw water injection pipe 3, a material for adding a material having a high specific gravity = 4, and a raw water injection pipe 5 flows from a mixing tank 2 into a coagulation and separation tank, and a raw water inlet 2a And a coagulant injection mouth raw water in the raw water into the °2a flow people. The coagulant is supplied to the population 2b for injecting coagulant 6. The mixing tank 2 maintains a full flow in the raw water for a certain residence time. The mixing tank 2 reacts the suspended matter in the raw water with the coagulating agent 6 to form a floc. In the construction 4 for adding a material having a high specific gravity, a screen 7 is installed to remove impurities in the raw water. A separator 8 is mounted above the structure 4 for adding a material having a high specific gravity. The material 9 having a high specific gravity is added from the separator 8 to the structure 4 for adding a material having a high specific gravity. The raw water injection pipe 5 is provided downstream of the structure 4 for adding a material having a high specific gravity. Coagulation aid ι〇 from the coagulation aid injection port 10a into the raw water injection pipe 5 Agent 1 〇 Make the material with high specific gravity 9 盥 、 疑 疑 疑 疑 、 、 、 、 U U U U U U U U ', 佚, 攸 produces a better solid-liquid separation. 105052.doc 1300006 In the mixing tank 2, a stirrer is preferably provided to form a turbulent flow, which is not shown in the figure. The raw water injection port 5a of the raw water injection pipe 5 is disposed so as to easily reach the turbulence floating in the coagulation and separation tank 1. The position of the screen 7 is not limited as long as it is located upstream of the coacervation and separation tank 1. However, to prevent the separator 8 from closing, the screen 7 is preferably provided upstream of the addition of the material 9 having a high specific gravity. Even if it is installed before the mixing tank 2, there is no problem. It goes without saying that if the raw water contains no impurities, it is not necessary to install the screen 7. The addition of the coagulation aid 10 and the material 9 having a high specific gravity is provided so that the material 9 having a high specific gravity and the coagulation aid 1 will simultaneously react to promote the formation of flocs. Although the position at which the material 9 having a high specific gravity is added may be located on the upstream side of the spin-on and separation tank 1, the material 9 having a high specific gravity is preferably added between the coagulation and separation tank 1 and the mixing tank 2. The position at which the coagulation aid 10 is added may be before the mixed liquid flows into the coacervation and separation tank 1. The location of the addition of the coagulating aid 10 may also be in the vicinity of the coagulation and separation tank 1 in the raw water injection port 5a after the injection of the mixed liquid, the coagulation aid 1 〇 directly mixed. A water flow generator 1 1 is provided in the middle of the depolymerization and separation tank 1 for disturbing the flowing mixed liquid (i.e., the liquid in which the raw water and the coagulant 6 are mixed), i.e., the water to be treated, to produce a water flow. An aquarium 12 is provided above the coagulation and separation tank for collecting treated water obtained by performing solid-liquid separation. The treated water is injected into the outside of the system from the sump J2 via the treated water outlet 丨2a. At the lower portion of the agglomerating and separating tank i, a dirt discharge port 13' is provided for discharging the dirt separated from the treated water. A dirt collection box 14 is provided on the lower side of the outer side of the coagulation and separation tank 1 for collecting sweat from the dirt discharge port 13. The dirt in the sweat collection box 14 is transferred to the separator 8 via a dirt transfer 105052.doc -11 - 1300006. One opening and closing valve 丨 6 and a transfer pump 丨 7 are sequentially disposed on one side of the dirt collecting box 14 on the dirt transfer keeper 15. The coagulation and separation tank 1A has a quality measuring instrument 18 for measuring the quality of the water at the interface κ. A water quality measuring instrument 18 is coupled to the opening and closing valve 16 to drive the opening and closing valve 16 based on signals from the water quality measuring instrument 18. The coagulation and separation tank i is preferably constructed in a cylindrical shape. However, the cohesive and separation tank 1 can be constructed as a cube (orthogonal parallelepiped) in consideration of efficient use of space and construction cost. Condensation and separation cans can be a polyhedron rather than a planar shape. In this case, it preferably has a shape of a polyhedron which is uniform and symmetrical. If the height and the short are compared in the case of the same capacity, the latter is not suitable for generating eddy current even in the case of the same capacity. Therefore, the height of the coagulation and separation tank 1 is preferably larger than the length (diameter or width) in the horizontal direction. In other words, if the shape of the agglomerating and separating tank 1 is a cylindrical body ', the ratio of the height to the diameter is set to 1 or more. The ratio of the height to the horizontal length is set to 1 or more if it has a constant angle parallel/face shape '. However, even if the coagulation and separation tanks are long in the horizontal direction, a spacer is disposed in the coagulation and separation tank 1 to produce a smooth thirst. In a similar case, if the diameter of the upper portion of the coagulation and separation tank 1 is larger than the diameter of the lower portion, the rate of rise of the vortex in the upper portion of the tank 1 can be slowed down as compared with the lower portion. Therefore, the dirt interface K can be effectively produced. The coagulant 6 uses an iron series having a large amount of ionic charge and an aluminum series inorganic coagulant. Polyaluminum chloride, aluminum sulfate, iron chloride, iron sulfate or the like can be used as such an inorganic coagulant. Then, the type of the coagulant 6 is not limited, and the floc can be sufficiently formed by the corpse 105052.doc -12-!3〇0〇〇6.

分離器8分離出自汙物轉移管15流出的凝聚汙物中的具 有高比重之材料9。分離器8重新利用具有高比重之材料 9°於該第-實施例中，分離器8構造成一旋液分離器。分 離器8將藉由分離獲得的具有高比重之材料9提供至用於 添加具有高比重之材料之構造4中。分離器8將其中剩餘之 汗物排放到系統外部。可使用其他類型的震置作為分離器 只要其能分離汙物與具有高比重之材料可使用分級 罐來剝離附著至具有高比重之材料9之汙物並將其藉由 (例如）授拌、混合或摔落等去除。不言㈣，若不重^利 用具有高比重之材料9’則具有高比重之材料9可與汙物一 起排放到系統外部。 向混合液體（生水與凝聚劑6混合之液體）中添加具有高 :重之材料9之目的係增加絮凝物之表觀比重。舉例而 =可使用具有一或多種細沙之比重的材料作為具有高比 重之材料9。細沙具有2 6 $ +舌 1 π ^ ^ ^ 之比重、17之均勻係數及約1〇〇 微米之有效粒徑。可使用具有接近細沙之比重且比重為2 至8的無機或有機材料。《可使用該材料與細沙之混合 物。具有高比重之材料9於驅動凝聚及分離 重範圍係2.0至3.0。石榴石、和幼之1且比 々牙田石、超級灰（super ash，由T〇ky〇The separator 8 separates the material 9 having a high specific gravity from the cohesive dirt flowing out of the dirt transfer pipe 15. The separator 8 reuses a material having a high specific gravity 9°. In this first embodiment, the separator 8 is constructed as a hydrocyclone. The separator 8 supplies the material 9 having a high specific gravity obtained by separation to the structure 4 for adding a material having a high specific gravity. The separator 8 discharges the remaining sweat therein to the outside of the system. Other types of vibration can be used as the separator as long as it can separate the dirt from the material having a high specific gravity, and the classification tank can be used to peel off the dirt attached to the material 9 having a high specific gravity and to, for example, mix it, Mix or drop and remove. Needless to say (4), if a material having a high specific gravity 9' is used, the material 9 having a high specific gravity can be discharged to the outside of the system together with the dirt. The purpose of adding a material having a high:heavy weight to the mixed liquid (the liquid in which the raw water is mixed with the coagulant 6) is to increase the apparent specific gravity of the floc. For example, a material having a specific gravity of one or more fine sands may be used as the material 9 having a high specific gravity. The fine sand has a specific gravity of 2 6 $ + tongue 1 π ^ ^ ^ , a uniform coefficient of 17 and an effective particle diameter of about 1 μm. An inorganic or organic material having a specific gravity close to that of fine sand and having a specific gravity of 2 to 8 can be used. "A mixture of this material and fine sand can be used. The material 9 having a high specific gravity drives the aggregation and separation weight range of 2.0 to 3.0. Garnet, and younger than 々 田 石, super ash (by T〇ky〇

Me—Us製造）、氧化結、無煙煤等可作為此類具有高比 重之材料9。另外’可使用諸如陰離子型或非離子型高分 子凝聚劑作為凝聚助劑丨〇。 水流發生器11構造成一用於形成一具有不破壞絮凝物 105052.doc -13- 1300006 之攪拌剪切力之湍流區域的構件。水流發生器⑽造成一 用於使微絮凝物與具有高比重之材料9等接觸以形成大絮 凝物之構件。水流發i器i j構造成一具有轴流式授掉葉片 lla之攪拌器。水流發生器u具有一傳動軸ub及一馬達 。傳動軸iib自攪拌葉片lla垂直向上延伸。馬達Uc運 轉以使傳動軸11_#。端視設施狀況，傳動轴llb可於水 平方向延伸。軸流式水流發生器i i於一小的靜壓下即可產 生=的排放里。不僅可使用具有軸流式攪拌葉片i丨a之攪 拌器而且可使用幫浦、風機、喷射器等作為水流發生器 儘笞水μ發生器11較佳係一可變旋轉型，但端視凝聚 及分離裝置之驅動條件，其可係一不變旋轉型。此外，可 使用能令人滿意地產生渦流之其他構件作為水流發生器 件11，例如喷射產生器件，如循環器。 在該第一實施例中，集水池12收納自凝聚罐丨溢出的處 理後的水以便去除處理後的水中之絮凝物。處理後的水經 由處理後的水之出口 12a轉移至系統外部。集水池12可具 有一過濾器件。該過濾器件可呈一旋轉盤形式。可使用具 有一過濾元件之過濾器件或一具有一分離膜之膜過濾器 件或一濾布。此外，其可係一適合於所處理水之性質之水 槽，例如一浸沒式水槽。此一集水池或水槽將隨後再予以 闡述。 提供汙物收集箱14之目的係自凝聚及分離罐丨抽吸出凝 聚的汙物，以便防止汙物介面κ上升，以防增加凝聚及分 離罐1中汙物之濃度。汙物收集箱14由一傾斜壁14a自凝聚 105052.doc -14- 1300006 罐1底部之外表面向上傾斜並延伸而形成。汙物收 集箱14接收來自位於凝聚及分離罐m傾斜壁14&amp;間之、于 物排入口13之凝聚汗物。在該第一實施例中，汙物收集箱 Η提供於凝聚及分離罐丨之外部下職^然而，該位置並 不限於外部，只要其並不擾亂渦流且若其適合於汙物之凝 b在汗㈣集箱14中’使凝聚汗物增厚以降低用於再循 核具有高比重之材料9之循環率及降低排放至系統外部之Me-Us manufacturing, oxidation, anthracite, etc. can be used as such a material having a high specific gravity. Further, an anionic or nonionic high molecular agglomerating agent can be used as the coagulation aid. The water flow generator 11 is constructed as a member for forming a turbulent flow region having a stirring shear force that does not damage the floccule 105052.doc -13- 1300006. The water flow generator (10) causes a member for contacting the microflocs with the material 9 having a high specific gravity or the like to form a large floc. The water flow generator i j is constructed as a stirrer having an axial flow type transfer blade lla. The water flow generator u has a drive shaft ub and a motor. The drive shaft iib extends vertically upward from the agitating blade 11a. The motor Uc is operated to drive the drive shaft 11_#. The drive shaft 11b can extend in the horizontal direction depending on the condition of the facility. The axial flow generator i i can generate a discharge under a small static pressure. It is possible to use not only a stirrer having an axial flow stirring blade i丨a but also a pump, a fan, an ejector or the like as a water flow generator. The water μ generator 11 is preferably a variable rotation type, but the end view is condensed. And the driving condition of the separating device, which can be a constant rotation type. Further, other members capable of satisfactorily generating eddy currents can be used as the water flow generator member 11, such as an injection generating device such as a circulator. In the first embodiment, the sump 12 houses the treated water overflowed from the condensed cans to remove the flocs in the treated water. The treated water is transferred to the outside of the system through the treated water outlet 12a. The sump 12 can have a filter device. The filter device can be in the form of a rotating disk. A filter device having a filter element or a membrane filter or a filter cloth having a separation membrane can be used. Further, it may be a water tank suitable for the nature of the water to be treated, such as a submerged water tank. This collection of sinks or sinks will be explained later. The purpose of providing the dirt collection box 14 is to extract the concentrated contaminants from the coagulation and separation tanks in order to prevent the contamination interface κ from rising to prevent an increase in the concentration of contaminants and separation of the contaminants in the tank 1. The dirt collection box 14 is formed by an inclined wall 14a self-condensing 105052.doc -14- 1300006. The outer surface of the bottom of the can 1 is inclined upward and extended. The dirt collection box 14 receives the agglomerated sweat from the object inlet 13 between the inclined walls 14 &amp; In the first embodiment, the dirt collection box Η is provided outside the condensing and separating tanks. However, the position is not limited to the outside as long as it does not disturb the eddy current and if it is suitable for the condensation of dirt. In the sweat (four) header 14 'to thicken the agglomerated sweat to reduce the circulation rate of the material 9 having a high specific gravity for re-nucleation and to reduce emissions to the outside of the system

汗物量。汙物收集箱14中之凝聚汙物藉助轉移幫浦Η抽吸 出。 汗物轉移管15經由打開及閉合闕16及轉移幫浦Η自汙 物收集箱14抽吸m于物1此汙物轉移f 15控制凝聚 及分離罐1中固體之密度。汙物轉移管15將抽吸出之凝聚 汗物提供至分離器8中。分離器8用於自凝聚汙物分離出具 有高比重之材料9並使之循環。換言之，將具有高比重之 材料9以一定濃度添加至生水中以使具有高比重之材料9 參與凝聚反應。根據藉助轉移幫浦17抽出的凝聚汙物之量 控制濃度。不言而喻’若不重新利用具有高比重之材料9, 則具有高比重之材料9可與凝聚汙物一起排放至系統外部 而無需安裝分離器8。 水品質量測儀器18持續地量測凝聚及分離罐艸絮凝物 之狀況。換言之’水品質量測儀器18監测凝聚及分離罐i 中絮凝物之過度積聚。水品質量測儀器18可構造為一介面 儀錄、濃度計或濁度計等。通常，當凝聚及分離罐】中絮 凝物濃度升高日夺，汙物介面K升高。水品質量測儀器㈣ 105052.doc 1300006 終對凝聚及分離罐1中之汙物介面K加以量測。若絮凝物過 度積聚，則水品質量測儀器1 8會自動開啟打開及閉合閥 16，將多餘絮凝物作為凝聚汙物抽出。因此，水品質量測 儀器18平衡凝聚及分離罐1中絮凝物之量並控制汙物介面 Κ，以便不使絮凝物流出至處理後的水一側。為持續監測 凝聚及分離罐1中絮凝物之狀況，不但可利用一種量測凝 聚及分離罐1中絮凝物狀況之方法，而且可利用一種量測 處理後的水之濁度或透明度之方法或利用兩種方法之組 合方法。 較佳始終將凝聚及分離罐1中水表面與汗物介面Κ間之 距離控制在1 ·0毫米或以上，以便令人滿意地運行該凝聚 及分離裝置。適宜情況係將汙物濃度調節至約7至14%。 換言之，較佳相對於流入之生水將凝聚汙物的抽吸量設定 為約3至1 0%。亦較佳情況係將凝聚及分離罐i中之濃度設 定為約0·5至3%。若要如此，需藉助打開及閉合閥16及轉 移幫浦17以一適宜之時間段自凝聚罐1抽吸出一定量之凝 聚汙物。另外，將該一定量之凝聚汙物經由汙物轉移管15 轉移至分離器8中。然後，在分離器8中自凝聚汙物分離出 具有高比重之材料9。剩餘之汙物排放至系統外部。由此， 可防止絮凝物流至處理後的水一側。防止了處理後的水劣 化。 接下來將闡述該第一實施例中凝聚及分離裝置之運 作。當凝聚劑6自凝聚劑注入口几與流入混合罐2中之生水 混合時，生水中之懸浮物質與凝聚劑6反應形成絮凝物。 105052.doc •16- 1300006 如此形成絮凝物之混合液體（生水與凝聚劑6混合之液體） 經由生水注入管3流入用於添加具有高比重之材料之構造 4中。在此期間，篩網7去除生水中之雜質並防止分離器8 閉合。在用於添加具有高比重之材料之構造4中，具有高 比重之材料9自分離器8混合入混合液體（生水與凝聚劑6 混合之液體）中。然後，該包含具有高比重之材料9之混合 液體（生水與凝聚劑6混合之液體）流入生水注入管5，在此 期間凝聚助劑10自凝聚助劑注入口 1 〇&amp;混合入該混合液體 (生水與凝聚劑6混合之液體）。 由此，包含材料9及凝聚助劑1〇之混合液體（生水與凝聚 劑6混合之液體）自生水注入口 5a流至凝聚及分離罐1中形 成擬處理水。在凝聚及分離罐1中，水流發生器丨丨運作以 在擬處理水中產生循環流或渦流。渦流之總量變成先前凝 聚及分離罐1中擬處理水與自生水注入口 5 a新加入的生水 之總和。該渦流在凝聚及分離罐1之中部變成下降流。繼 而該渦流於凝聚及分離罐1之底部變成水平流（徑向流）。 此後，該渦流變成一上升流。進一步地，該渦流於靠近介 面K處變成一水平流（向心流）。此一渦流使懸浮物質與具 有高比重之材料9及凝聚助劑10反應，藉此高效地產生絮 凝物。與具有高比重之材料9結合之絮凝物顯示出高表觀 比重。換言之，由於絮凝物於凝聚及分離罐1中之循環速 率較擬處理水之上升速度快’其沉降而形成汙物介面。然 後，下部之凝聚汙物經由汙物排放出口 13流出，到達汗物 收集箱14。上部之處理後的水溢出至集水池12。由此，在 105052.doc -17- 1300006 凝聚及分離罐1中絮凝物之形成與固體_液體分離同時進 行。 在此期間，汙物收集箱14中之凝聚汙物經由汙物轉移管 15流至分離器8中，同時水品質量測儀器18量測凝聚及分 離罐1中汙物介面尺處水之品質以向打開及閉合閥1 6輸出 信號。換言之，為保持凝聚及分離罐丨中具有高比重之材 料9相對於擬處理水之濃度，水品質量測儀器“改變打開 及閉合閥16之開口以將凝聚及分離罐丨中之多餘絮凝物作 為凝聚汙物抽吸出來，藉此平衡凝聚及分離罐丨中絮凝物 之篁。分離器8自凝聚汙物分離出具有高比重之材料9。分 離器8使具有高比重之材料9返回用於添加具有高比重之 材料之裝置4。 該第一實施例之凝聚及分離裝置利用使用凝聚劑6之絮 凝物之形成並利用來自水流發生器丨〗之渦流。因此該凝聚 及分離裝置可在丨個凝聚及分離罐丨中連續實施絮凝物分 離製私因此，不需要除傳統凝聚反應罐以外的固體-液 體分離罐。此可降低所需的空間。在此一構造中，由於提 仏此合罐2以將凝聚劑6混合入生水中，故可高效地混合凝 聚劑6與生水並迅速使生水中可靠地形成絮凝物。另外， 由於在/4、加具有鬲比重之材料9處的上游提供筛網7，故可 防止分離器8堵塞並可穩定地提高凝聚及分離罐1中凝聚 之效率。由於分離器8構造成旋液分離器，故可阻止設施 成本之增加。由於向混合液體（生水與凝聚劑6混合之液 體）中’々、加具有南比重之材料9，故可形成大的絮凝物並提 105052.doc -18- 1300006 面處理速率。 第二實施例 圖2係一方塊圖，其顯示本發明凝聚及分離裝置之第二 實施例。重複的闡述内容將省略。相同的參考數字指示與 圖1所不實施例相同的部件。在該第二實施例之凝聚及分 離裝置中，於凝聚及分離罐1之中部提供一導流管21。靠 ..............-—........---------------—’ 近汙物介面水平佈置一多i元件22。另外，於多孔元件22 下’在凝聚及分離罐1之内表面上提供一導流板23。凝聚 及分離罐1之罐形狀為矩形。 、一^ 在該第二實施例中，水流發生器丨丨之垂直位置係在導流 管21之中部。攪拌葉片Ua之水平位置係在導流管21之底 部。必須在導流管21中攪拌前供應具有高比重之材料9。 因此’生水注入管5之生水注入口 5a較佳提供於導流管21 内側或直接位於導流管2 1之上，以便包含具有高比重之材 料9及凝聚助劑10之混合液體（生水與凝聚劑6混合之液 體）將容易地漂浮於在導流管2 1中移動之渦流之上。妙 而右生水谷易地漂浮於渴流之上，則生水注入管5之生 水注入口 5a之位置可位於導流管21中，在導流管21之下部 區域或在導流管21之上部區域。此外，生水注入管$之生 水注入口 5a可自其中水流發生器11之傳動軸1113穿過多孔 元件22之切口部分引入。 導流管2 1之形狀為圓柱形，於垂直方向上具有開口，此 系為便於製造及降低成本。詳言之，導流管2丨由一錐形圓 管形成，其中導流管2 1下部之開口之直徑較其上部開口 105052.doc -19- 1300006 大。換言之’其由一具有圓錐外形之圓管形成，以便容易 地使渦流自下降流改變成水平流（徑向流）。若導流管21内 則水平剖面與導流管21外側水平剖面一致，則可形成穩定 的渦流並促成固體·液體令人滿意地分離。導流管21之形 狀並無限制’只要其結構能使其可容易地使渦流自下降流 改變成水平流（徑向流），即其結構可使其幫助液流產生渦 流。其可係一中心孔或一套管等、一接近圓形之多面體、 或朝向其下部增寬及增厚之圓錐外形。 凝聚及分離罐1之底面與導流管2丨之底面間的距離較佳 係水ML發生器11之攪拌葉片11 a直徑的約7 5 %。水流發生器 11之攪拌葉片11 a之垂直位置較佳不自導流管2 i伸出，儘 官其如上所述位於導流管21之下部。然而，導流管2丨之攪 拌葉片1 la之垂直位置並無限制，只要其可提供有效的渦 流。 多孔元件22可代替該第一實施例之水品質量測儀器 18，例如一具有無數開口之平板。安裝多孔元件“係為了 穩定地形成汙物介面，防止絮凝物向上流出，移除紊亂地 處理的水，產生直流，由此可獲得優質且穩定的處理後的 水。換言之，多孔元件22垂直地分割凝聚及分離罐j之内 部，可容易地於多孔元件22之上產生直流，並容易地於多 孔元件之下產生备、凝物形成區域（汙物區域）。可使用穿孔 金屬、網狀物、直流板、傾斜板、狹縫、蜂窩狀元件等作 為此類多孔元件22。 若平板、網狀物或穿孔金屬用於多孔元件22，則可不連 105052.doc -20- 1300006 績地提供一個以上的多孔元件22。儘管多孔元件22構造成 一平面，但可使用其他凸起或凹進形狀，舉例而言。另外， 可根據生水之性質改變多孔元件22之開口。舉例而言，若 多孔元件22之開口為50%，則集水池12之水槽之設施場所 佔地較佳為多孔元件22設施場所佔地的1/2或以下。換言 之’處理後的水通過多孔元件22之速率可與處理後的水升 至除水槽外的水表面上的速率相同或較其低。 導流板23將於凝聚及分離罐1之内表面與導流管21之外 表面間產生的上升流用阻礙效應平穩地改變成水平流（向 心流）。導流板23為一環形平板，其自凝聚及分離罐！之内 表面水平伸出。在該第二實施例之凝聚及分離裝置中，可 僅藉助水流發生器11來產生渦流。然而，為有政地產生可 靠而穩定的渦流，同時提供導流管21及導流板23。特定而 言’若凝聚及分離罐1之形狀具有角，例如一四角形，則 提供導流板23時，較佳使導流板23水平。若凝聚及分離罐 1具有一圓形，則較佳提供導流板23，用於穩定產生渦流 並防止滿流形成共旋。另外，較佳同時在水平及垂直方向 上提供導流板23。該類導流板23可係曲面板而非平板。 接下來將闡述該第二實施例之凝聚及分離裝置之運 作。自生水注入口 5a流入導流管2 1之生水，即生水與凝聚 劑6、具有高比重之材料9及凝聚助劑1〇混合之擬處理水立 即藉助水流發生器丨丨攪拌。然後，導流管2丨中之水流發生 $ 11攪拌擬處理水，形成湍流狀態。由此形成具有高比重 之絮凝物。繼而，擬處理之水流於導流管2丨之下部變成下 105052.doc -21 - 1300006 降流’於其下端變成水平流（徑向流），並於凝聚及分離罐 1之内表面與導流管21之外表面間變成垂直上升流。於導 流官2 1中產生之下降流使該上升流於導流管2丨之上端與 多孔元件22間變成水平流（向心流）。絮凝物漂浮於此一渦 流上並再次轉移至導流管21。在此期間，導流板23幫助渦 流容易地自上升流轉變成水平流（向心流）。由此形成汙物 介面。處理後的水通過多孔元件22並溢出至集水池12。 此外，假定處理後的水通過多孔元件22之速率為V。若 在凝聚及分離罐1中於以速率V上升的擬處理水下產生速 率較速率V大之水平流或下降流，則甚至沉降速率較速率 V小之絮凝物亦漂浮於該水平流或下降流上。由於其速率 較南’故很難漂浮於上升流上。換言之，由於絮凝物受到 來自涡流的較大力量，其自上升流移開。因此，即使絮凝 物以較上升速率V小之沉降速率移動，其亦可受到固體_ 液體分離。可分離小凝聚及分離罐1中之絮凝物。 為用渦流實施有效的固體-液體分離，較佳形成小而重 的絮凝物，即質量大而流動阻力小的重絮凝物。在該第二 實施例中，由於向混合液體（生水與凝聚劑6混合的液體） 中添加具有高比重之材料9及凝聚助劑1 〇，故固體-液體分 離效率提高。由於絮凝物較重，故凝聚及分離罐1下部之 絮凝物濃度升高。凝聚部件中絮凝物間之碰撞次數及粗顆 粒與絮凝物間之碰撞次數增加。凝聚效果提高。由此可小 型化該裝置。 因此’該第二實施例之凝聚及分離裝置可促進固體-液 105052.doc -22· 1300006 體分離過程而不會使絮凝物因重力而沉降。此藉由相對於 擬處理水之上升流速增大渦流（其藉由水流發生器丨丨之攪 拌產生）即於凝聚及分離罐1之内表面與導流管21之上端 間產生的水平流（向心流）之流速達成。此外，對包含具有 兩比重之材料9及凝聚助劑10之擬處理水於剛好流入凝聚 及分離罐1中後加以攪拌。然後，可均勻地分散凝聚助劑 10。添加具有咼比重之材料9使擬處理水中之膠狀物質或 懸浮物質環繞具有高比重之材料9形成大的絮凝物。因 此，可更有效地實施固體-液體分離。此外，在2或3分鐘 内可達成移除率為80%或以上的移除。在此情況下，必須 相對於流入水（生水，不包含凝聚劑6之擬處理水）以一定 /辰度於絮凝物中包含具有高比重之材料9。因此，相對於 流入水之量所添加之濃度較佳設定為3,〇〇〇至5,〇〇〇毫克/ 公升。然而，端視水品質或水的諸如黏度等性質，可改變 添加濃度。 第三實施例 圖3係一主方塊圖，其顯示本發明凝聚及分離裝置之第 三實施例。重複的闡述内容將省略。相同的參考數字指示 與圖2所示實施例相同的部件。類似於該第一實施例，在 該第二實施例中分離器8使用旋流分離器。然@，該第三 實施例中&lt; 分離器31藉助重力的影響自來自汙物轉移管 1 5之汗物分離出具有高比重 ^ 置之材枓9，亚使分離的高比重 之材料9返回用於添加呈右古μ舌 刀，、有呵比重之材料之構造4。分離器 3 1具有用於接收自汙物轅銘总 刃锝移官15流出的汙物的罐32。在罐 105052.doc -23 - 1300006 32中’自汙物轉移管15流出的汙物中具有相對重的重量的 高比重材料9受重力影響而沉降。具有相對輕的重量的高 比重材料9自罐32上部溢出。在罐32中沉降的具有高比重 之材料9供應至用於添加具有高比重之材料之構造4。自罐 32/jnL出之汙物轉移至系統外部。在該第三實施例之分離器 31中，具有高比重之材料9之沉降速率為約7〇米/小時，而 汙物之沉降速率為約3至4米/小時。與汙物之沉降速率相 比，具有高比重之材料9之沉降速率極大。因此，可在短 至約5分鐘的時間内藉助重力的影響分離具有高比重之材 料9。即使在該第三實施例之凝聚及分離裝置中亦可獲得 類似於該第二實施例之效果。 第四實施例 圖4係一主方塊圖，其顯示本發明凝聚及分離裝置之第 四實施例。重複的闡述内容將省略。相同的參考數字指示 與圖2所示實施例相同的部件。在該第四實施例中，導流 板23之内端佈置的較其外端高。藉此，在該第四實施例之 凝聚及分離裝置中，可獲得類似於該第二實施例之效果。 此外’可平穩地將在導流管21之外表面與凝聚及分離罐i 之内表面間流動的上升流改變成水平流（向心流）。 第五實施例 圖5係一主方塊圖，其顯示本發明凝聚及分離裝置之第 五實施例。重複的闡述内容將省略。相同的參考數字指示 與圖2所示實施例相同的部件。在該第五實施例中，具有 咼比重之材料9於凝聚助劑注入口 1 〇 a之下游側注入至生 105052.doc -24- 1300006 水注入管5中。因此，在該第二實施例中用於添加具有高 比重之材料之構造4構造成僅具有蒒網7之生水接收罐 4 A。即使在該第五實施例之凝聚及分離裝置中，亦可獲得 類似於該第二實施例之效果。添加凝聚助劑1〇之位置可係 混合液體流入凝聚及分離罐1中之前。然而，可剛好於靠 近凝聚及分離罐1中生水注入口 5a注入混合液體後將其與 凝聚助劑10混合。 第六實施例 II 圖6係一主方塊圖，其顯示本發明凝聚及分離裝置之第 六實施例。重複的闡述内容將省略。相同的參考數字指示 與圖2所示實施例相同的部件。在該第六實施例中，具有 高比重之材料9直接倒入凝聚及分離罐1中。在此情況下， 靠近生水注入管5a佈置一用於自分離器8提供具有高比重 之材料之開口 8a，以便具有高比重之材料9將在導流2 1管 中可靠地漂浮於渦流之上。出於該目的，用於添加具有高 比重之材料之構造4構造成僅具有篩網7之生水接收罐 ® 4 A。即使在該第六實施例之凝聚及分離裝置中，亦可獲得 類似於該第二實施例之效果。 第七實施例 圖7係一主方塊圖，其顯示本發明凝聚及分離裝置之第 七實施例。重複的闡述内容將省略。相同的參考數字指示 與圖2所示實施例相同的部件。在該第七實施例中，生水 注入管5之中間部分化於流動方向上向下傾斜。另外，具 有高比重之材料9及凝聚助劑1 0供應至生水注入管5之中 105052.doc -25- 1300006 間部分5b之最下端。因此，該帛二實施例之用於添加具有 尚比重之材料之構造4構造成僅具有筛網7之生水接收罐 4A。該第七實施例之凝聚及分離裝置可獲得類似於該第二 實施例之效果，並藉助生水注入管5之傾斜中間部分讣加 速生水之流動，從而加速導流管2丨中渦流之流動。 第八實施例 圖8係一主方塊圖，其顯示本發明凝聚及分離裝置之第 八實施例。重複的闡述内容將省略。相同的參考數字指示 與圖2所示實施例相同的部件。在該第八實施例中生水注 入管5之生水注入口 5 a自凝聚及分離罐1水平地引入導流 管21中。詳言之，生水注入管5穿過凝聚及分離罐i之側壁 及導流管21之側壁，以便包含具有高比重之材料9及凝聚 助劑10之混合液體（生水與凝聚劑6混合的液體）將在導流 管21中可靠地漂浮於渦流之上。在該第八實施例之凝聚及 分離罐中，可獲得類似於該第二實施例之效果。此外，其 可防止水平注入的生水受到阻礙流出而不能有效地形成 絮凝物。 第九實施例 圖9係一主方塊圖，其顯示本發明凝聚及分離裝置之第 九實施例。重複的闡述内容將省略。相同的參考數字指示 與圖1所示實施例相同的部件。在該第九實施例中，僅將 導流管21加至該第一實施例之凝聚及分離裝置中。在此情 況下，生水注入管5之生水注入口 5a之位置及水流發生器 11之位置類似於該第二實施例中彼等之位置。在該第九實 105052.doc -26- 1300006 施例之凝聚及分離裝置中，可獲得類似於該第一實施例之 效果。此外，藉助導流管21可令人滿意地形成渦流。 第十實施例 圖10係一主方塊圖，其顯示本發明凝聚及分離裝置之第 十實施例。重複的闡述内容將省略。相同的參考數字指示 與圖1所示實施例相同的部件。在該第十實施例中，僅導 流管21加至該第一實施例之凝聚及分離裝置中，而略去該 第一實施例之水品質量測儀器1 8。另外，提供管41、罐42 _ 及管43。管41用於抽出汙物以控制汙物介面K之高度。罐 42用於猎助重力的影響分離自管41流出的汙物。管43用於 將在罐42中獲得的上層清水返回凝聚及分離罐1。因此， 佈置管41之内端以便抽出汗物介面κ處之汙物並將沉降於 罐42中之汙物排放至系統外部。即使在該第十實施例之凝 聚及分離裝置中，亦可獲得類似於該第一實施例之效果。 此外，藉助導流管21可令人滿意地形成渦流。 第十一實施例 _ 圖11係一主方塊圖，其顯示本發明凝聚及分離裝置之第 十一實施例。重複的闡述内容將省略。相同的參考數字指 示與圖1所示實施例相同的部件。在該第十一實施例中， 僅導流管21加至該第一實施例之凝聚及分離裝置中。另 外’於凝聚及分離罐1中提供具有一過濾裝置之集水池 12 A，代替該第一實施例之集水池丨2。即使在該第^^一實 施例之凝聚及分離裝置中，亦可獲得類似於該第一實施例 之效果。此外，藉助導流管2 1可令人滿意地形成渦流。另 105052.doc -27- 1300006 外，藉助集水池12A可移除低品質的處理後的水。 第十二實施例The amount of sweat. The condensed dirt in the dirt collection box 14 is sucked out by means of the transfer pump. The sweat transfer tube 15 draws m from the dirt collection box 14 via the opening and closing rafts 16 and the transfer rafts. The dirt transfer f 15 controls the concentration of solids in the condensed and separated tanks 1. The dirt transfer pipe 15 supplies the sucked coagulated sweat to the separator 8. The separator 8 is used to separate and circulate the material 9 having a high specific gravity from the coagulated dirt. In other words, the material 9 having a high specific gravity is added to the raw water at a concentration to cause the material 9 having a high specific gravity to participate in the aggregation reaction. The concentration is controlled in accordance with the amount of condensed dirt extracted by the transfer pump 17. It goes without saying that if the material 9 having a high specific gravity is not reused, the material 9 having a high specific gravity can be discharged to the outside of the system together with the cohesive dirt without installing the separator 8. The water quality measuring instrument 18 continuously measures the condition of coagulation and separation of the cans and flocs. In other words, the 'water quality measuring instrument 18 monitors the excessive accumulation of flocs in the coagulation and separation tank i. The water quality measuring instrument 18 can be constructed as an interface meter, a concentration meter or a turbidimeter. Generally, when the flocculation concentration in the coagulation and separation tank is increased, the soil interface K is increased. Water quality measuring instrument (4) 105052.doc 1300006 Finally, the dirt interface K in the coagulation and separation tank 1 is measured. If the floc is excessively accumulated, the water quality measuring instrument 18 will automatically open the opening and closing valve 16, and the excess floc will be extracted as a cohesive dirt. Therefore, the water quality measuring instrument 18 balances the amount of flocs in the coagulation and separation tank 1 and controls the dirt interface Κ so as not to cause the flocculation to flow out to the treated water side. In order to continuously monitor the condition of flocculation and separation of the floc in the tank 1, it is possible to use not only a method for measuring the condition of flocculation and separation of the floc in the tank 1, but also a method for measuring the turbidity or transparency of the treated water or A combination of the two methods is utilized. It is preferable to always control the distance between the water surface in the coagulation and separation tank 1 and the sweat interface to be 1.0 mm or more in order to satisfactorily operate the coagulation and separation device. Suitably, the soil concentration is adjusted to about 7 to 14%. In other words, it is preferable to set the suction amount of the coagulated dirt to about 3 to 10% with respect to the raw water flowing in. It is also preferred to set the concentration in the coacervation and separation tank i to about 0.5 to 3%. To do so, a certain amount of contaminant dirt is sucked from the coagulation tank 1 by means of the opening and closing valve 16 and the transfer pump 17 for a suitable period of time. In addition, a certain amount of the cohesive dirt is transferred to the separator 8 via the dirt transfer pipe 15. Then, the material 9 having a high specific gravity is separated from the coagulated dirt in the separator 8. The remaining dirt is discharged to the outside of the system. Thereby, the flocculation stream can be prevented from flowing to the treated water side. Prevents deterioration of water after treatment. Next, the operation of the agglomeration and separation apparatus in the first embodiment will be explained. When the coagulant 6 is mixed with the raw water flowing into the mixing tank 2 from the coagulant injection port, the suspended matter in the raw water reacts with the coagulating agent 6 to form a floc. 105052.doc • 16-1300006 The mixed liquid in which the flocs are formed (the liquid in which the raw water and the coagulant 6 are mixed) flows into the structure 4 for adding a material having a high specific gravity through the raw water injection pipe 3. During this time, the screen 7 removes impurities in the raw water and prevents the separator 8 from closing. In the structure 4 for adding a material having a high specific gravity, the material 9 having a high specific gravity is mixed from the separator 8 into a mixed liquid (liquid in which raw water and agglomerating agent 6 are mixed). Then, the mixed liquid containing the material 9 having a high specific gravity (the liquid in which the raw water and the coagulant 6 are mixed) flows into the raw water injection pipe 5, during which the coagulation aid 10 is mixed from the coagulation aid injection port 1 〇 & The mixed liquid (liquid in which raw water and agglomerating agent 6 are mixed). Thus, the mixed liquid containing the material 9 and the coagulation aid 1 (the liquid in which the raw water and the coagulant 6 are mixed) flows from the raw water injection port 5a to the coagulation and separation tank 1 to form the treated water. In the coagulation and separation tank 1, the water flow generator 丨丨 operates to generate a circulating flow or eddy current in the water to be treated. The total amount of eddy currents becomes the sum of the newly added raw water in the previous condensation and separation tank 1 and the spontaneous water injection port 5 a. This eddy current becomes a downward flow in the middle of the agglomeration and separation tank 1. Then, the eddy current becomes a horizontal flow (radial flow) at the bottom of the coagulation and separation tank 1. Thereafter, the eddy current becomes an upflow. Further, the eddy current becomes a horizontal flow (central flow) near the interface K. This eddy current reacts the suspended matter with the material 9 having a high specific gravity and the coagulation aid 10, thereby efficiently generating flocs. The floc combined with the material 9 having a high specific gravity exhibits a high apparent specific gravity. In other words, since the flocculation rate in the coagulation and separation tank 1 is faster than that of the treated water, it settles to form a dirt interface. Then, the lower aggregated dirt flows out through the dirt discharge outlet 13 to the sweat collecting box 14. The treated water from the upper portion overflows into the sump 12. Thus, the formation of flocs in the coagulation and separation tank 1 is carried out simultaneously with the solid-liquid separation in 105052.doc -17-1300006. During this period, the condensed dirt in the dirt collection tank 14 flows to the separator 8 via the dirt transfer pipe 15, and the water quality measuring instrument 18 measures the quality of the water at the dirt interface of the condensing and separating tank 1. The signal is output to the opening and closing valve 16. In other words, in order to maintain the concentration of the material 9 having a high specific gravity in the agglomerated and separated tanks relative to the concentration of the water to be treated, the water quality measuring instrument "changes the opening of the opening and closing valve 16 to coagulate and separate excess flocs in the tank. The coagulated dirt is sucked out to balance the coagulation and separation of the floc in the can. The separator 8 separates the material having a high specific gravity from the coagulated dirt. The separator 8 returns the material 9 having a high specific gravity. The apparatus 4 for adding a material having a high specific gravity. The agglomeration and separation apparatus of the first embodiment utilizes the formation of flocs using the coagulant 6 and utilizes the eddy current from the water flow generator. Therefore, the coagulation and separation device can Continuously performing flocculation separation and separation in a coagulation and separation tank. Therefore, there is no need for a solid-liquid separation tank other than the conventional coagulation reaction tank. This can reduce the required space. In this configuration, The can 2 is mixed with the coagulant 6 into the raw water, so that the coagulant 6 and the raw water can be efficiently mixed and the floc can be reliably formed in the raw water. In addition, since The screen 7 is provided upstream of the material 9 having a specific gravity, so that the separator 8 can be prevented from being clogged and the efficiency of agglomeration and agglomeration in the separation tank 1 can be stably improved. Since the separator 8 is constructed as a hydrocyclone, it can be prevented. The increase in the cost of the facility. Since the mixed liquid (the liquid in which the raw water is mixed with the coagulant 6) is added to the material 9 having a south specific gravity, a large floc can be formed and treated 105052.doc -18-1300006 Second Embodiment Fig. 2 is a block diagram showing a second embodiment of the agglomeration and separation apparatus of the present invention, and the repeated description will be omitted. The same reference numerals denote the same components as those of the embodiment of Fig. 1. In the coagulation and separation device of the second embodiment, a draft tube 21 is provided in the middle of the coagulation and separation tank 1. By..............--..... ...----------------'The near-dirty interface is horizontally arranged with a multi-i element 22. In addition, under the porous element 22' on the inner surface of the coagulation and separation tank 1 A baffle 23 is provided. The shape of the can of the coagulation and separation tank 1 is rectangular. In the second embodiment, the water flow generator 丨The vertical position is in the middle of the draft tube 21. The horizontal position of the stirring blade Ua is at the bottom of the draft tube 21. The material having a high specific gravity must be supplied before the stirring in the draft tube 21. Therefore, the raw water injection tube The raw water injection port 5a is preferably provided inside the draft tube 21 or directly above the draft tube 21 to contain a mixed liquid of the material 9 having a high specific gravity and the coagulation aid 10 (raw water and coagulant 6) The mixed liquid) will easily float above the vortex flowing in the draft tube 2 1. The right water valley easily floats above the thirsty flow, and the raw water injection port 5 is placed at the raw water injection port 5a. It may be located in the draft tube 21, in the lower region of the draft tube 21 or in the upper portion of the draft tube 21. Further, the raw water injection port 5a of the raw water injection pipe may be from the drive shaft 1113 of the water flow generator 11 therein. Introduced through the slit portion of the porous member 22. The draft tube 21 has a cylindrical shape and has an opening in the vertical direction for ease of manufacture and cost reduction. In detail, the draft tube 2 is formed by a tapered tube, wherein the opening of the lower portion of the draft tube 2 1 has a larger diameter than the upper opening 105052.doc -19-1300006. In other words, it is formed by a circular tube having a conical shape to easily change the eddy current from the descending flow to the horizontal flow (radial flow). If the horizontal section in the draft tube 21 coincides with the horizontal cross section on the outer side of the draft tube 21, a stable vortex can be formed and the solid/liquid can be satisfactorily separated. The shape of the draft tube 21 is not limited as long as it is structured such that it can easily change the eddy current from the downflow to the horizontal flow (radial flow), i.e., its structure allows it to assist the flow to generate eddy currents. It can be a central hole or a sleeve, etc., a nearly circular polyhedron, or a conical shape that widens and thickens toward its lower portion. The distance between the bottom surface of the coagulation and separation tank 1 and the bottom surface of the draft tube 2 is preferably about 75 % of the diameter of the stirring blade 11 a of the water ML generator 11. The vertical position of the agitating blades 11a of the water flow generator 11 preferably does not extend from the flow guiding tube 2i, and is disposed at the lower portion of the draft tube 21 as described above. However, the vertical position of the stirring blade 1 la of the draft tube 2 is not limited as long as it provides an effective eddy current. The porous member 22 can be substituted for the water quality measuring instrument 18 of the first embodiment, such as a flat plate having a myriad of openings. The porous element is mounted "in order to stably form a dirt interface, prevent flocculation from flowing upward, remove turbulently treated water, generate direct current, thereby obtaining high quality and stable treated water. In other words, the porous member 22 is vertically By dividing the inside of the agglomerating and separating tank j, it is possible to easily generate a direct current on the porous member 22, and to easily generate a preparation and a condensate forming region (a dirt region) under the porous member. Perforated metal or mesh can be used. a DC plate, a slanting plate, a slit, a honeycomb element, or the like as such a porous member 22. If a flat plate, a mesh, or a perforated metal is used for the porous member 22, it may be provided without a 105052.doc -20-1300006 The above porous member 22. Although the porous member 22 is constructed in a flat shape, other convex or concave shapes may be used, for example, in addition, the opening of the porous member 22 may be changed depending on the nature of the raw water. For example, if porous If the opening of the component 22 is 50%, the installation space of the water tank of the sump 12 is preferably 1/2 or less of the space occupied by the porous component 22 facility. In other words, The rate at which water passes through the porous member 22 may be the same as or lower than the rate at which the treated water rises to the surface of the water other than the sink. The deflector 23 will converge the inner surface of the canister 1 and the draft tube 21 The upward flow generated between the outer surfaces is smoothly changed into a horizontal flow (central flow) by the obstruction effect. The baffle 23 is an annular flat plate which protrudes horizontally from the inner surface of the coagulation and separation tank! In this second embodiment In the condensing and separating device, the eddy current can be generated only by the water flow generator 11. However, in order to produce a reliable and stable eddy current, the draft tube 21 and the deflector 23 are provided at the same time. The shape of the separation tank 1 has an angle, for example, a square shape. When the baffle 23 is provided, the baffle 23 is preferably horizontal. If the coagulation and separation tank 1 has a circular shape, the baffle 23 is preferably provided. The eddy current is stably generated and the full flow is prevented from forming the co-rotation. Further, it is preferable to simultaneously provide the baffle 23 in the horizontal and vertical directions. The baffle 23 can bend the panel instead of the flat plate. Coagulation and separation device of the embodiment The raw water injection port 5a flows into the raw water of the draft tube 2, that is, the raw water and the coagulant 6, the material having the high specific gravity 9 and the coagulation aid 1〇 are mixed, and the water is immediately stirred by the water flow generator. Then, the water flow in the draft tube 2 is stirred by the water to generate a turbulent state, thereby forming a turbulent state, thereby forming a floc having a high specific gravity. Then, the water to be treated flows down the lower portion of the draft tube 2 to the lower 105052. .doc -21 - 1300006 The downflow 'becomes a horizontal flow (radial flow) at its lower end and becomes a vertical upward flow between the inner surface of the condensation and separation tank 1 and the outer surface of the draft tube 21. The descending flow generated in 1 causes the upward flow to become a horizontal flow (central flow) between the upper end of the draft tube 2 and the porous member 22. The flocs float on this vortex and are again transferred to the draft tube 21. During this time, the baffles 23 help the eddy currents to easily transition from an upflow to a horizontal flow (central flow). This forms a dirt interface. The treated water passes through the porous element 22 and overflows into the sump 12. Further, it is assumed that the rate at which the treated water passes through the porous member 22 is V. If in the agglomeration and separation tank 1 a horizontal flow or a downward flow rate is generated at a rate V greater than the rate at which the rate V rises, even a floc having a sedimentation rate smaller than the velocity V floats in the horizontal flow or falls. On the flow. It is difficult to float on the upflow because of its souther rate. In other words, since the floc is subjected to a large force from the eddy current, it is removed from the upward flow. Therefore, even if the floc moves at a sedimentation rate lower than the ascending rate V, it can be separated by the solid-liquid. The small agglomerates and the flocs in the separation tank 1 can be separated. In order to carry out effective solid-liquid separation by eddy currents, it is preferred to form small and heavy flocs, i.e., heavy floes of high mass and low flow resistance. In the second embodiment, since the material 9 having a high specific gravity and the coagulation aid 1 are added to the mixed liquid (the liquid in which the raw water and the coagulant 6 are mixed), the solid-liquid separation efficiency is improved. Since the flocs are heavy, the flocculation concentration in the lower portion of the flocculation and separation tank 1 is increased. The number of collisions between the flocs in the agglomerated part and the number of collisions between the coarse particles and the flocs increase. The cohesion effect is improved. This makes it possible to miniaturize the device. Therefore, the agglomeration and separation apparatus of the second embodiment can promote the solid-liquid 105052.doc-22·1300006 body separation process without causing the flocs to settle due to gravity. This is caused by increasing the eddy current (which is generated by the agitation of the water flow generator) with respect to the rising flow rate of the water to be treated, that is, the horizontal flow generated between the inner surface of the coagulation and separation tank 1 and the upper end of the draft tube 21 ( The flow rate to the heart flow is reached. Further, the water to be treated containing the material 9 having two specific gravities and the coagulation aid 10 is just stirred into the coagulation and separation tank 1, and then stirred. Then, the coagulation aid 10 can be uniformly dispersed. The addition of the material 9 having a helium specific gravity causes the colloidal or suspended matter in the water to be treated to form a large floc around the material 9 having a high specific gravity. Therefore, the solid-liquid separation can be carried out more efficiently. In addition, removal with a removal rate of 80% or more can be achieved in 2 or 3 minutes. In this case, it is necessary to contain the material 9 having a high specific gravity in the floc at a certain/time with respect to the inflowing water (raw water, the treated water not containing the coagulant 6). Therefore, the concentration added relative to the amount of influent water is preferably set to 3, 〇〇〇 to 5, 〇〇〇 mg / liter. However, depending on the nature of the water or the nature of the water such as viscosity, the concentration of addition can be varied. THIRD EMBODIMENT Fig. 3 is a main block diagram showing a third embodiment of the agglomeration and separation apparatus of the present invention. Duplicate elaboration will be omitted. The same reference numerals indicate the same components as the embodiment shown in Fig. 2. Similar to this first embodiment, the separator 8 uses a cyclone separator in this second embodiment. However, in the third embodiment, the separator 31 separates the material having a high specific gravity from the sweat from the dirt transfer pipe 15 by the influence of gravity, and the high-specific gravity material 9 is separated. Return to the structure 4 for adding a material with a right-handed tongue. The separator 3 1 has a tank 32 for receiving contaminants flowing out of the dirt. In the tank 105052.doc -23 - 1300006 32, the high specific gravity material 9 having a relatively heavy weight in the dirt flowing out of the dirt transfer pipe 15 is settled by the influence of gravity. The high specific gravity material 9 having a relatively light weight overflows from the upper portion of the tank 32. The material 9 having a high specific gravity settled in the tank 32 is supplied to the structure 4 for adding a material having a high specific gravity. The dirt from the tank 32/jnL is transferred to the outside of the system. In the separator 31 of the third embodiment, the sedimentation rate of the material 9 having a high specific gravity is about 7 Å/hr, and the sedimentation rate of the dirt is about 3 to 4 m/hr. The sedimentation rate of the material 9 having a high specific gravity is extremely large as compared with the sedimentation rate of the dirt. Therefore, the material 9 having a high specific gravity can be separated by the influence of gravity in a period of as short as about 5 minutes. Even in the agglomeration and separation apparatus of the third embodiment, effects similar to those of the second embodiment can be obtained. Fourth Embodiment Fig. 4 is a main block diagram showing a fourth embodiment of the agglomeration and separation apparatus of the present invention. Duplicate elaboration will be omitted. The same reference numerals indicate the same components as the embodiment shown in Fig. 2. In the fourth embodiment, the inner end of the deflector 23 is disposed higher than the outer end thereof. Thereby, in the agglomeration and separation apparatus of the fourth embodiment, effects similar to those of the second embodiment can be obtained. Further, the upward flow flowing between the outer surface of the draft tube 21 and the inner surface of the coagulation and separation tank i can be smoothly changed into a horizontal flow (central flow). [Fifth Embodiment] Fig. 5 is a main block diagram showing a fifth embodiment of the agglomeration and separation apparatus of the present invention. Duplicate elaboration will be omitted. The same reference numerals indicate the same components as the embodiment shown in Fig. 2. In the fifth embodiment, the material 9 having a specific gravity of helium is injected into the raw material 105052.doc -24-1300006 water injection pipe 5 on the downstream side of the coagulation aid injection port 1 〇 a . Therefore, the configuration 4 for adding a material having a high specific gravity in the second embodiment is configured to have only the raw water receiving tank 4 A of the mesh 7. Even in the agglomeration and separation apparatus of the fifth embodiment, effects similar to those of the second embodiment can be obtained. The position at which the coagulation aid is added may be before the mixed liquid flows into the coagulation and separation tank 1. However, it is possible to mix the mixed liquid with the coagulation aid 10 just after the mixed liquid is injected into the raw water injection port 5a in the coagulation and separation tank 1. Sixth Embodiment II Fig. 6 is a main block diagram showing a sixth embodiment of the agglomeration and separation apparatus of the present invention. Duplicate elaboration will be omitted. The same reference numerals indicate the same components as the embodiment shown in Fig. 2. In the sixth embodiment, the material 9 having a high specific gravity is directly poured into the coagulation and separation tank 1. In this case, an opening 8a for supplying a material having a high specific gravity from the separator 8 is disposed adjacent to the raw water injection pipe 5a, so that the material 9 having a high specific gravity will reliably float in the eddy current in the flow guiding tube on. For this purpose, the construction 4 for adding a material having a high specific gravity is constructed as a raw water receiving tank ® 4 A having only the screen 7. Even in the agglomeration and separation apparatus of the sixth embodiment, effects similar to those of the second embodiment can be obtained. Seventh Embodiment Fig. 7 is a main block diagram showing a seventh embodiment of the agglomeration and separation apparatus of the present invention. Duplicate elaboration will be omitted. The same reference numerals indicate the same components as the embodiment shown in Fig. 2. In the seventh embodiment, the middle portion of the raw water injection pipe 5 is inclined downward in the flow direction. Further, the material 9 having a high specific gravity and the coagulating aid 10 are supplied to the lowermost end of the portion 5b between the 105052.doc - 25- 1300006 in the raw water injection pipe 5. Therefore, the structure 4 for adding a material having a specific gravity in the second embodiment is constructed as a raw water receiving tank 4A having only the screen 7. The agglomeration and separation device of the seventh embodiment can obtain an effect similar to that of the second embodiment, and accelerates the flow of raw water by means of the inclined intermediate portion of the raw water injection pipe 5, thereby accelerating the eddy current in the draft tube 2 flow. Eighth Embodiment Fig. 8 is a main block diagram showing an eighth embodiment of the agglomeration and separation apparatus of the present invention. Duplicate elaboration will be omitted. The same reference numerals indicate the same components as the embodiment shown in Fig. 2. In the eighth embodiment, the raw water injection port 5a of the raw water injection pipe 5 is horizontally introduced into the draft tube 21 from the coagulation and separation tank 1. In detail, the raw water injection pipe 5 passes through the side wall of the agglomerating and separating tank i and the side wall of the draft tube 21 to contain a mixed liquid of the material 9 having a high specific gravity and the coagulation aid 10 (raw water is mixed with the coagulant 6). The liquid) will reliably float above the vortex in the draft tube 21. In the coagulation and separation tank of the eighth embodiment, effects similar to those of the second embodiment can be obtained. Further, it prevents the horizontally injected raw water from being hindered from flowing out and cannot effectively form flocs. Ninth Embodiment Fig. 9 is a main block diagram showing a ninth embodiment of the agglomeration and separation apparatus of the present invention. Duplicate elaboration will be omitted. The same reference numerals indicate the same components as the embodiment shown in Fig. 1. In the ninth embodiment, only the draft tube 21 is added to the agglomeration and separation apparatus of the first embodiment. In this case, the position of the raw water injection port 5a of the raw water injection pipe 5 and the position of the water flow generator 11 are similar to those of the second embodiment. In the agglomeration and separation apparatus of the ninth embodiment 105052.doc -26-1300006, an effect similar to that of the first embodiment can be obtained. Furthermore, the eddy current can be satisfactorily formed by means of the draft tube 21. Tenth Embodiment Fig. 10 is a main block diagram showing a tenth embodiment of the agglomeration and separation apparatus of the present invention. Duplicate elaboration will be omitted. The same reference numerals indicate the same components as the embodiment shown in Fig. 1. In the tenth embodiment, only the draft tube 21 is added to the coagulation and separation device of the first embodiment, and the water quality measuring instrument 18 of the first embodiment is omitted. Further, a tube 41, a tank 42_, and a tube 43 are provided. The tube 41 is used to extract dirt to control the height of the dirt interface K. The tank 42 is used for hunting the influence of gravity to separate the dirt flowing out of the tube 41. The tube 43 is for returning the supernatant water obtained in the tank 42 to the agglomeration and separation tank 1. Therefore, the inner end of the tube 41 is arranged to extract the dirt at the sweat interface κ and discharge the dirt settled in the tank 42 to the outside of the system. Even in the polymerization and separation apparatus of the tenth embodiment, effects similar to those of the first embodiment can be obtained. Furthermore, the eddy current can be satisfactorily formed by means of the draft tube 21. Eleventh Embodiment Fig. 11 is a main block diagram showing an eleventh embodiment of the agglomeration and separation apparatus of the present invention. Duplicate elaboration will be omitted. The same reference numerals indicate the same components as the embodiment shown in Fig. 1. In the eleventh embodiment, only the draft tube 21 is added to the agglomeration and separation device of the first embodiment. Further, a sump 12 A having a filtering device is provided in the condensing and separating tank 1 instead of the sump 2 of the first embodiment. Even in the agglomeration and separation apparatus of the first embodiment, effects similar to those of the first embodiment can be obtained. Furthermore, the eddy current can be satisfactorily formed by means of the draft tube 2 1 . Another 105052.doc -27-1300006, the low quality treated water can be removed by means of the sump 12A. Twelfth embodiment

圖12係一主方塊圖，其顯示本發明凝聚及分離裝置之第 十二實施例。重複的闡述内容將省略。相同的參考數字指 示與圖1所示實施例相同的部件。在該第十二實施例，僅 導流管21加至該第一實施例之凝聚及分離裝置中。於凝聚 及分離罐1之外部k供一具有過渡裝置之集水池12 A，代替 該第一實施例之集水池12。即使在該第十二實施例之凝聚 及分離裝置中，亦可獲得類似於該第一實施例之效果。此 外，藉助導流管21可充分地形成渦流。 第十三實施例 圖13係一主方塊圖，其顯示本發明凝聚及分離裝置之第 十三實施例。重複的闡述内容將省略。相同的參考數字指 示與圖2所示實施例相同的部件。在該第十三實施例中， 長:供一管路混合器5 1來代替該第二實施例中之混合罐2。 管路混合器51包含一導管及一螺旋槳。該導管之孔徑與生 水流入口 2a或生水注入管相同，舉例而言。該螺旋槳佈置 於該導管中。若要形成絮凝物，僅需將凝聚劑6注入生水 中，即使管路混合器51僅具有導管而無螺旋槳。然而，為 令人滿意地形成絮凝物，較佳使用一結構簡單的靜止混合 器來在其内部產生渦流，以促進攪拌，進行混合。可給出 由NIHON INKA有限公司製造的WES丁fall_inka靜止注 射混合器2800型作為此一實例。即使在該第十三實施例之 凝聚及分離裝置中，亦可獲得類似於該第二實施例之效 105052.doc -28- 1300006 果。 因此，在第三至第十三實施例中闡述導流管2丨主要與圓 形凝聚及分離罐1 一起提供。然而，如圖14中所示，可提 供複數個串接的矩形凝聚及分離罐1A並在每一凝聚及分 離罐1A中提供導流管21。藉此，可處理獨立反應或流入物 改變的情況。另外，如圖15所示，可以一矩形形式佈置四 個矩形凝聚及分離罐1A。亦可於每一凝聚及分離罐ία中 佈置導流管2 1。另外，如圖丨6所示，可成直線地佈置複數 個八邊形凝聚及分離罐1B。如圖1 7所示，可以蜂窩結構方 式佈置複數個六邊形凝聚及分離罐1B。另外，可在1個凝 聚及分離罐1B中佈置複數個導流管，以使其相互之間不幹 擾，但此構型未示出。在此一情況下，其需與水流發生器 等的性質相平衡。 第二至第八及第十三實施例闡述導流板23水平或實質 水平長:供。然而，導流板23之形狀或方向並不限於上述形 狀，只要導流板23可有效地產生渦流。特定而言，若凝聚 及分離罐1具有一圓柱形或具有一極類似於圓柱形的形 狀，則較佳垂直提供複數個導流板23A，以防止渦流發生 共旋，如圖18所示。換言之，較佳以有規律的間隔於圓形 凝聚及分離罐1之内表面上水平提供複數個（例如4個）導 流板23A。在此一情況下，導流板23A藉由一阻礙效應將 由水流發生裔11之攪拌效應產生的水平渦流改變成垂直 流，以便於向上的方向整理擬處理水之流動。該類垂直導 流板23A可與1個凝聚及分離罐丨以及水平導流板23 一起提 105052.doc -29- 1300006 供。在此情況下，可有助於藉助鸯直導流板23 A整理上升 流並藉助水平導流板23整理水平流（向心流）。然而，若凝 聚及分離罐1係多面體，則由於内表面限制共旋，故有時 無需提供垂直導流板23A。 若在第一及第十三實施例中，集水池12使用一浸沒式水 槽’則可使用一具有在三角形管61 a之上部縱向延伸之開 口 61b的水槽61，如圖19所示。另外，可使用一具有在圓 形管62a之上部縱向延伸之開口 62b的水槽62，如圖20所 不。另外，可使用一具有無數個於縱向上直線佈置於圓形 管63 a上部之小孔63b的水槽63，如圖21所示。另外，可採 用一將複數個三角形水槽64合併在一起的結構，如圖22 所不。或者’可使用一具有傾斜表面65a的水槽65，如圖 23中所示，但其並非浸沒式。 若諸如生水之濃度等性質之變化特別大，且若當量測汙 物介面K及凝聚及分離罐i中之濃度時處理變得不穩定，則 可使用一集水池12B。在集水池12B中，一過濾材料66〇或 未圖不之繞直板等安裝於具有垂直表面66a之箱66b 上如圖24所不。或者，可使用一集水池12c。在集水池 12C中，一過濾材料67c安裝於具有傾斜表面之箱6几 上，如圖25所示。另外，亦可藉由提供過遽材料66c、67c ;集水池12上賦予過濾、功能，如圖24、25所示。在此情況 下，過濾、材料66c、67c可使用比重為1〇或以下的球形過 慮材，。$而，即使過渡材料具有1〇或以上的比重，其 /Λ 17藉由在過濾材料底部佈置一篩網等以類似方式使 105052.doc -30- 1300006 用。較佳藉助氣動提升作用等連續地實施循環沖刷，以將 所捕集的汙物作為沖刷排放物排放到系統外部。另一方 面，若生水之性質改變並不很大，則對於集水池12可使用 一具有等距離佈置的垂直或傾斜平板之矯直板來代替過 濾材料66c、67c。通常，使用水槽61至65來收集來自水或 水表面之上層清水較適宜，如圖19至23所示。或者，適宜 情況係使用一未圖示之管道。其可根據生水等的性質使 實施圖1所示凝聚及分離裝置之第一實施例。作為實施 條件，使用汙水處理廠中第一沉降池之流入水作為生水。 以10毫克/公升之添加速率向生水中添加PAC(由Al2〇3轉 化）以形成凝聚劑（無機凝聚劑）6。以3,〇〇〇毫克/公升之濃 度向生水中添加沙子，形成具有高比重之材料9。以丨毫克 /公升之濃度向生水中添加高分子凝聚劑，形成凝聚助劑 1 〇。於該條件下，獲得關於流入水量、裝置停留時間、生 水SS、處理後的水之ss、ss移除率、汙物濃度及抽吸出 的汙物之量間關係的結果，如表i所示。由表i可看出，當 裂置之停留時間為10分鐘時，ss移除率變為8〇%或以上。 由此可獲得具有良好品質之處理後的水。對於以8〇%或以 上的SS移除率移除，裝置之停留時間變短。此乃因水品質 量測儀器18對汙物表面加以平衡，同時具有高比重之材料 9之添加可有效地促進凝聚而形成重絮凝物，藉此渦流於 105052.doc -31 - 1300006 短時間内形成汙物介面κ。 表1 圖 1裝置之結果 流入水 裝置停留 生水SS 處理後的水之 SS移 汙物濃度 抽吸出的汙 之量（米3/ 時間（分鐘） (毫克/公 SS(毫克/公 除率 (毫克/公 物量 小時） 升） 升） (%) 升） (米V小時） 12.5 30 231 32 86 3?628 0.75 37.5 10 304 52 83 4,532 2.25 75 5 253 76 70 3,306 4.5 第二實例 實施圖2所示凝聚及分離裝置之第二實施例。實施條件 類似於該第一實施例。於該條件下，獲得關於流入水量、 裝置停留時間、生水SS、處理後的水之SS、SS移除率、 汙物濃度及抽吸出的汙物之量間關係的結果，如表2所 示。由表2可看出，當裝置之停留時間為3分鐘時，SS移除 率變為80%或以上。由此可獲得具有良好品質之處理後的 水。對於以80%或以上的SS移除率移除，裝置之停留時間 變短。此乃因導流管21有郊地促進絮凝物之凝聚而形成重 絮凝物，藉此渦流於短時間内形成汙物介面Κ。 表2 圖2裝置之結果 流入水之 量(米3/ 小時） 裝置停留 時間 (分鐘） 生水SS (毫克/ 公升） 處理後的水 之SS (毫克/公升） SS移除率 (%) 汙物濃度 (毫克/ 公升） 抽吸出的汙 物量（米3/ 小時） 37.5 10 303 18 94 5,040 2.25 75 5 212 19 91 3,507 4.5 125 3 193 21 89 3,159 7.5 105052.doc •32- 1300006 【圖式簡單說明】 圖1之方塊圖顯示本發明凝聚及分離裝置之第一實施 例。 圖2之方塊圖顯示本發明凝聚及分離裝置之第二實施 例。 圖3之主方塊圖顯示本發明凝聚及分離裝置之第三實施 例。 圖4之主方塊圖顯示本發明凝聚及分離裝置之第四實施 例0 圖5之主方塊圖顯示本發明凝聚及分離裝置之第五實施 例。 圖6之主方塊圖顯示本發明凝聚及分離裝置之第六實施 例。 圖7之主方塊圖顯示本發明凝聚及分離裝置之第七實施 例。 圖8之主方塊圖顯示本發明凝聚及分離裝置之第八實施 例0 圖9之主方塊圖顯示本發明凝聚及分離裝置之第九實施 例。 圖10之主方塊圖顯示本發明凝聚及分離裝置之第十實 施例。 圖11之主方塊圖顯示本發明凝聚及分離裝置之第十一 實施例。 圖12之主方塊圖顯示本發明凝聚及分離裝置之第十二 105052.doc -33- 1300006 實施例。 圖13之主方塊圖顯示本發明凝聚及分離裝置 實施例。 之第十三 圖14之平面圖顯示佈置複數個凝聚及分離襄置 圖15之平面圖顯示佈置複數個凝聚及分離较置之衩式。 圖16之平面圖顯示佈置複數個凝聚及分離裴置之极武。 圖17之平面圖顯示佈置複數個凝聚及分離裝置之极式。 圖1 8之平面圖顯示佈置一導流板之模式。 之权式。 圖19之透視圖顯示一用於一集水池之水槽。 圖20之透視圖顯示一用於一集水池之水槽。 圖21之透視圖顯示一用於一集水池之水槽。 圖22之部分剖面圖顯示一用於一集水池之水槽。 圖23之部分剖面圖顯示一用於一集水池之水槽。 圖24之部分剖面圖顯示一使用一過濾材料之水槽。 圖25之部分剖面圖顯示一使用一過濾材料之水槽。 【主要元件符號說明】 1 凝聚及分離罐 1A 凝聚及分離罐 1B 凝聚及分離罐 2 混合罐 2a 生水流入口 2b 凝聚劑注入口 3 生水注入管 4 用於添加具有高比重之材料的構造 105052.doc -34- 1300006 4A 生水接收罐 5 生水注入管 5a 生水注入口 5b 生水注入管 6 凝聚劑 7 篩網 8 分離器 8a 提供具有高 9 具有高比重 10 凝聚助劑 10a 凝聚助劑注 11 水流發生器 11a 轴流式攪拌 lib 傳動軸 11c 馬達 12 集水池 12a 處理後水的 12A 集水池 12B 集水池 12C 集水池 13 汙物排放口 14 汙物收集箱 14a 汙物收集箱 15 汙物轉移管Figure 12 is a main block diagram showing a twelfth embodiment of the agglomeration and separation apparatus of the present invention. Duplicate elaboration will be omitted. The same reference numerals indicate the same components as the embodiment shown in Fig. 1. In the twelfth embodiment, only the draft tube 21 is added to the agglomeration and separation apparatus of the first embodiment. Instead of the sump 12 of the first embodiment, a sump 12 A having a transition device is provided outside the condensing and separating tank 1. Even in the coagulation and separation device of the twelfth embodiment, effects similar to those of the first embodiment can be obtained. Further, the eddy current can be sufficiently formed by the draft tube 21. Thirteenth Embodiment Fig. 13 is a main block diagram showing a thirteenth embodiment of the agglomeration and separation apparatus of the present invention. Duplicate elaboration will be omitted. The same reference numerals denote the same components as the embodiment shown in Fig. 2. In the thirteenth embodiment, the length: a line mixer 51 is used in place of the mixing tank 2 in the second embodiment. The line mixer 51 includes a conduit and a propeller. The diameter of the conduit is the same as that of the raw water inlet 2a or the raw water injection tube, for example. The propeller is disposed in the conduit. To form flocs, it is only necessary to inject the coagulant 6 into the raw water even if the in-line mixer 51 has only a conduit and no propeller. However, in order to satisfactorily form flocs, it is preferred to use a simple static mixer to generate eddy currents therein to promote agitation and mixing. As an example, a WES Ding fall_inka static injection mixer Model 2800 manufactured by NIHON INKA Co., Ltd. can be given. Even in the condensing and separating apparatus of the thirteenth embodiment, effects similar to those of the second embodiment 105052.doc -28-1300006 can be obtained. Therefore, it is explained in the third to thirteenth embodiments that the draft tube 2丨 is mainly provided together with the circular agglomeration and separation tank 1. However, as shown in Fig. 14, a plurality of tandem rectangular condensing and separating tanks 1A may be provided and a draft tube 21 may be provided in each of the condensing and separating tanks 1A. Thereby, it is possible to handle the case of independent reaction or influx change. Further, as shown in Fig. 15, four rectangular condensing and separating tanks 1A may be arranged in a rectangular form. The draft tube 2 1 can also be arranged in each of the cohesive and separation tanks ία. Further, as shown in Fig. 6, a plurality of octagonal condensation and separation tanks 1B may be arranged in a line. As shown in Fig. 17, a plurality of hexagonal condensation and separation tanks 1B can be arranged in a honeycomb structure. Further, a plurality of draft tubes may be arranged in one of the condensation and separation tanks 1B so as not to interfere with each other, but this configuration is not shown. In this case, it needs to be balanced with the properties of the water flow generator and the like. The second to eighth and thirteenth embodiments illustrate the horizontal or substantial horizontal length of the deflector 23: for supply. However, the shape or direction of the deflector 23 is not limited to the above shape as long as the deflector 23 can effectively generate eddy currents. Specifically, if the coagulation and separation tank 1 has a cylindrical shape or a shape similar to a cylindrical shape, it is preferable to provide a plurality of baffles 23A vertically to prevent co-rotation of the eddy current, as shown in Fig. 18. In other words, a plurality of (e.g., four) baffles 23A are preferably provided horizontally at regular intervals on the inner surface of the circular agglomeration and separation can 1 . In this case, the deflector 23A changes the horizontal eddy current generated by the stirring effect of the water flow generation to a vertical flow by a hindrance effect, so as to align the flow of the water to be treated in the upward direction. This type of vertical baffle 23A can be supplied with a coagulation and separation tank and a horizontal baffle 23, 105052.doc -29-1300006. In this case, it is possible to assist in sorting the upflow by means of the straight deflector 23 A and collating the horizontal flow (central flow) by means of the horizontal baffle 23. However, if the coagulation and separation tank 1 is a polyhedron, since the inner surface restricts the co-rotation, it is sometimes unnecessary to provide the vertical baffle 23A. In the first and thirteenth embodiments, the sump 12 uses a submerged water tank' to use a water tank 61 having an opening 61b extending longitudinally above the triangular tube 61a, as shown in Fig. 19. Alternatively, a water tank 62 having an opening 62b extending longitudinally above the upper portion of the circular tube 62a can be used, as shown in Fig. 20. Further, a water tank 63 having an infinite number of small holes 63b arranged linearly in the upper portion of the circular tube 63a in the longitudinal direction can be used, as shown in Fig.21. Alternatively, a structure in which a plurality of triangular water tanks 64 are merged together may be employed, as shown in Fig. 22. Alternatively, a water tank 65 having an inclined surface 65a can be used, as shown in Fig. 23, but it is not submerged. If the change in properties such as the concentration of raw water is particularly large, and if the treatment becomes unstable when the concentration of the interface K and the concentration in the agglomerating and separating tank i is equal, a sump 12B can be used. In the sump 12B, a filter material 66 or a straight plate or the like which is not shown is attached to the case 66b having the vertical surface 66a as shown in Fig. 24. Alternatively, a collection basin 12c can be used. In the sump 12C, a filter material 67c is attached to the case 6 having an inclined surface as shown in Fig. 25. In addition, filtration and function can be provided on the sump 12 by providing the ruthenium materials 66c, 67c, as shown in Figs. In this case, the filter, the material 66c, 67c may use a spherical material having a specific gravity of 1 Torr or less. And, even if the transition material has a specific gravity of 1 Torr or more, the / Λ 17 is used in a similar manner by arranging a screen or the like at the bottom of the filter material. 105052.doc -30-1300006 is used. The cyclic flushing is preferably carried out continuously by means of a pneumatic lifting action or the like to discharge the trapped dirt as a flushing discharge to the outside of the system. On the other hand, if the nature of the raw water does not change much, the sump 12 may be replaced with a vertical or inclined flat plate having an equidistant arrangement instead of the filter materials 66c, 67c. In general, it is preferable to use the water tanks 61 to 65 to collect water from the upper surface of the water or water surface, as shown in Figs. Alternatively, a pipe (not shown) is used as appropriate. The first embodiment of the agglomeration and separation apparatus shown in Fig. 1 can be carried out depending on the nature of raw water or the like. As an implementation condition, the inflow water of the first settling tank in the sewage treatment plant is used as raw water. PAC (converted from Al2?3) was added to raw water at an addition rate of 10 mg/liter to form a coagulant (inorganic coagulant) 6. Sand is added to the raw water at a concentration of 3, 〇〇〇mg/liter to form a material 9 having a high specific gravity. A polymer flocculant is added to the raw water at a concentration of 丨mg/liter to form an agglomeration aid 1 〇. Under this condition, the results of the relationship between the amount of influent water, the residence time of the apparatus, the raw water SS, the ss of the treated water, the removal rate of the ss, the concentration of the dirt, and the amount of the sucked dirt are obtained. Shown. As can be seen from Table i, when the residence time of the rupture is 10 minutes, the ss removal rate becomes 8 〇% or more. Thus, treated water having good quality can be obtained. For removal at an SS removal rate of 8% or more, the residence time of the device becomes shorter. This is because the water quality measuring instrument 18 balances the surface of the dirt, and the addition of the material 9 having a high specific gravity can effectively promote coagulation to form heavy flocs, thereby vortexing at 105052.doc -31 - 1300006 in a short time. A dirt interface κ is formed. Table 1 Figure 1 Results of the device Inflow water device staying raw water SS The amount of sewage absorbed by the SS transfer concentration of water after treatment (m 3 / time (minutes) (mg / g SS (mg / mn rate) (mg/h, hour) liter) liter) (%) liter) (meter V hour) 12.5 30 231 32 86 3?628 0.75 37.5 10 304 52 83 4,532 2.25 75 5 253 76 70 3,306 4.5 Second example implementation Figure 2 A second embodiment of the coagulation and separation device shown. The implementation conditions are similar to the first embodiment. Under this condition, the results of the relationship between the amount of influent water, the residence time of the apparatus, the raw water SS, the SS of the treated water, the SS removal rate, the concentration of the contaminant, and the amount of the contaminant extracted are obtained. Shown. As can be seen from Table 2, when the residence time of the apparatus was 3 minutes, the SS removal rate became 80% or more. Thus, treated water having good quality can be obtained. For removal at an SS removal rate of 80% or more, the residence time of the device becomes shorter. This is because the subduct of the draft tube 21 promotes the agglomeration of flocs to form heavy flocs, whereby the eddy current forms a foul interface in a short time. Table 2 Figure 2 The result of the device influx of water (m3 / hour) Device residence time (minutes) Raw water SS (mg / liter) SS of treated water (mg / liter) SS removal rate (%) Concentration (mg/L) The amount of dirt pumped out (m3/hour) 37.5 10 303 18 94 5,040 2.25 75 5 212 19 91 3,507 4.5 125 3 193 21 89 3,159 7.5 105052.doc •32- 1300006 BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a block diagram showing a first embodiment of the agglomeration and separation apparatus of the present invention. Figure 2 is a block diagram showing a second embodiment of the agglomeration and separation apparatus of the present invention. The main block diagram of Fig. 3 shows a third embodiment of the agglomeration and separation apparatus of the present invention. The main block diagram of Fig. 4 shows a fourth embodiment of the agglomeration and separation apparatus of the present invention. The main block diagram of Fig. 5 shows a fifth embodiment of the agglomeration and separation apparatus of the present invention. The main block diagram of Fig. 6 shows a sixth embodiment of the agglomeration and separation apparatus of the present invention. The main block diagram of Fig. 7 shows a seventh embodiment of the agglomeration and separation apparatus of the present invention. The main block diagram of Fig. 8 shows an eighth embodiment of the agglomeration and separation apparatus of the present invention. Fig. 9 is a main block diagram showing a ninth embodiment of the agglomeration and separation apparatus of the present invention. The main block diagram of Fig. 10 shows a tenth embodiment of the agglomeration and separation apparatus of the present invention. The main block diagram of Fig. 11 shows an eleventh embodiment of the agglomeration and separation apparatus of the present invention. The main block diagram of Figure 12 shows an embodiment of the twelfth 105052.doc-33-1300006 of the present invention. The main block diagram of Figure 13 shows an embodiment of the agglomeration and separation apparatus of the present invention. Thirteenth Figure 14 is a plan view showing the arrangement of a plurality of condensing and separating devices. The plan view of Figure 15 shows the arrangement of a plurality of condensing and separating squats. The plan view of Figure 16 shows the extremes of arranging a plurality of coacervating and separating devices. Figure 17 is a plan view showing the arrangement of a plurality of agglomeration and separation devices. The plan view of Fig. 18 shows the mode in which a baffle is arranged. The right form. Figure 19 is a perspective view showing a sink for a pool. Figure 20 is a perspective view showing a sink for a pool. Figure 21 is a perspective view showing a sink for a pool. Figure 22 is a partial cross-sectional view showing a sink for a sump. Figure 23 is a partial cross-sectional view showing a sink for a sump. Figure 24 is a partial cross-sectional view showing a sink using a filter material. Figure 25 is a partial cross-sectional view showing a sink using a filter material. [Description of main components] 1 Condensation and separation tank 1A Condensation and separation tank 1B Condensation and separation tank 2 Mix tank 2a Raw water inlet 2b Coagulant injection port 3 Raw water injection pipe 4 Structure for adding material with high specific gravity 105052 .doc -34- 1300006 4A Raw water receiving tank 5 Raw water injection pipe 5a Raw water injection port 5b Raw water injection pipe 6 Coagulant 7 Screen 8 Separator 8a Provides high 9 with high specific gravity 10 Coagulation aid 10a Coagulation aid Agent Note 11 Water flow generator 11a Axial flow stirring lib Drive shaft 11c Motor 12 Water collection tank 12a Water treatment 12A Water collection tank 12B Water collection tank 12C Water collection tank 13 Contamination discharge port 14 Contamination collection box 14a Contamination collection box 15 Transfer tube

5之中間部分 比重之材料之開口 之材料 入口 10a 葉片 出口 之傾斜壁 105052.doc -35- 1300006Intermediate part of 5 material of the opening of the specific gravity material inlet 10a blade outlet inclined wall 105052.doc -35- 1300006

16 打開及閉合閥 17 轉移幫浦 18 水品質量測儀器 21 導流管 22 多孔元件 23 導流板 23A 導流板 31 分離器 32 用於接收自汙物轉移管流出之汙物的罐 41 管 42 罐 43 管 51 管路混合器 61 水槽 61a 三角形管 61b 在三角形管之上部縱向延伸之開口 62 水槽 62a 圓形管 62b 在圓形管上縱向延伸之開口 63 水槽 63a 圓形管 63b 小孔 64 三角形水槽 65 水槽 105052.doc -36- 1300006 65a 傾斜表面 66a 垂直表面 66b 箱 66c 過遽材料 67a 傾斜表面 67b 箱 67c 過濾材料 K 汙物介面 -37- 105052.doc16 Open and close valve 17 Transfer pump 18 Water quality measuring instrument 21 Guide tube 22 Porous element 23 Guide plate 23A Guide plate 31 Separator 32 Tank 41 for receiving dirt from the dirt transfer tube 42 tank 43 tube 51 line mixer 61 sink 61a triangular tube 61b opening 62 extending longitudinally above the triangular tube sink 62a circular tube 62b opening 63 extending longitudinally on the circular tube sink 63a circular tube 63b small hole 64 Triangle sink 65 sink 105052.doc -36- 1300006 65a inclined surface 66a vertical surface 66b box 66c through material 67a inclined surface 67b box 67c filter material K dirt interface -37- 105052.doc

Claims (1)

13 〇〇§©634072ttft 乃年日修(更)正替換頁; 包含生水及凝聚劑之 中文申請專利範圍替換本(97年5月） 十、申請專利範圍： 1# 一種凝聚及分離裝置，其包含： 一凝聚及分離罐，其用於盛裝一 液體混合物； 導机g，其上下端具有開口，並設置於該凝聚及分 離罐内之中央； 導管，其係將該液體混合物引導至該導流管； 水机發生器，其設置於該導流管内，用以使該液體 此合物於該導流管内向下方流動，以使該液體混合物於 該凝聚及分離罐内產生渦流； 一汙物收集箱，其係設置於該凝聚及分離罐外側，用 於引導凝聚污物通過設置於該凝聚及分離罐下部之污 物排放口，以便濃縮或增稠該凝聚汙物及 一汙物轉移構件，其係用於轉移於該汙物收集箱所濃 縮或增稠之該凝聚汙物。 2·如請求項1之凝聚及分離裝置，其中一具有高比重之材 料供至該凝聚及分離罐内。 3·如請求項2之凝聚及分離裝置，其中該汙物轉移構件連 接至一用於自該凝聚汙物分離該具有高比重之材料的 分離器。 4. 如請求項1至3中任一項之凝聚及分離裝置，其中在該凝 聚及分離罐内的該導流管之上端上方設置有_多孔元 件。 5. 如請求項1至3中任一項之凝聚及分離裝置，其中該水流 105052-970519.doc 1300006 μ 0听修(更)正朁換頁 發生器係一具有一軸流式攪拌葉片之授〜 6·如請求項1至3中任一項之凝聚及分離裝置，其中提供一 管路混合器以混合该凝聚劑與該生水，以便製備該^體 混合物。 7.如請求項1至3中任一項之凝聚及分離裝置，其中在該凝 聚及分離罐處設置有一水品質量測構件。 8·如請求項1至3中任一項之凝聚及分離裝置，其中在該凝 5^及分離罐之上部提供一集水池’用於捕集於該凝聚及 分離罐中處理的水並將該處理後的水自該凝聚及分離 罐輸送出來。13 〇〇§©634072ttft is the annual replacement (more) replacement page; Chinese patent application scope including raw water and coagulant replacement (May 97) X. Patent application scope: 1# A coagulation and separation device, The method comprises: a coagulation and separation tank for containing a liquid mixture; a guide g having an opening at an upper end thereof and disposed in a center of the coagulation and separation tank; and a conduit guiding the liquid mixture to the a water conduit generator disposed in the draft tube for flowing the liquid compound downward in the draft tube to cause the liquid mixture to generate eddy currents in the coagulation and separation tank; a dirt collection box disposed on the outside of the coagulation and separation tank for guiding the cohesive dirt through a dirt discharge port disposed at a lower portion of the coagulation and separation tank to concentrate or thicken the cohesive dirt and a contaminant A transfer member for transferring the condensed dirt concentrated or thickened by the dirt collection box. 2. The agglomeration and separation device of claim 1, wherein a material having a high specific gravity is supplied to the coagulation and separation tank. 3. The coacervation and separation device of claim 2, wherein the dirt transfer member is coupled to a separator for separating the material having a high specific gravity from the cohesive contaminant. 4. The agglomeration and separation apparatus of any one of claims 1 to 3, wherein a perforated element is disposed above the upper end of the draft tube in the condensation and separation tank. 5. The agglomeration and separation device of any one of claims 1 to 3, wherein the water flow 105052-970519.doc 1300006 μ 0 is a modified (more) positive page changer generator having an axial flow mixing blade The agglomeration and separation apparatus according to any one of claims 1 to 3, wherein a line mixer is provided to mix the coagulant with the raw water to prepare the mixture. 7. The agglomeration and separation apparatus of any one of claims 1 to 3, wherein a water quality measuring member is disposed at the condensation and separation tank. The agglomeration and separation apparatus according to any one of claims 1 to 3, wherein a pool is provided on the upper portion of the condensation tank and the separation tank for trapping water treated in the condensation and separation tank and The treated water is transported from the coagulation and separation tank. 105052-970519.doc 2- &lt; ； 13〇〇_06134〇72號專利申請案 中文圖式替換本(97年5月） 十一、圖式：105052-970519.doc 2- &lt;; 13〇〇_06134〇72 Patent Application Chinese Graphic Replacement (May 97) XI. Schema: 91 蟈 qcsl «Z 105052-970519-fig.doc 1300006 _____ ‘ 日修(更)正替換頁丨91 蝈 qcsl «Z 105052-970519-fig.doc 1300006 _____ ‘Day repair (more) is replacing page 丨 τ cdCN -2- 105052-970519-fig.doc 1300006 汙物τ cdCN -2- 105052-970519-fig.doc 1300006 105052-970519-fig.doc 1300006105052-970519-fig.doc 1300006 105052-970519-fig.doc -4- 1300006 I - 一1 卜年Γ/彳〖A (更:)正'IH奐頁I105052-970519-fig.doc -4- 1300006 I - A 1 Bu Γ / 彳 A (more:) 正 'IH 奂 page I 圖6Figure 6 105052-970519-fig.doc 1300006 11C 12105052-970519-fig.doc 1300006 11C 12 105052-970519-fig.doc 1300006 %年厂月 &lt;日修(更)正替換頁丨105052-970519-fig.doc 1300006 %年厂月&lt;日修(more) is replacing page丨 11C11C 11C11C 圖11 105052-970519-fig.doc I --------1300006 卜严C7K斤晴更)正替換百 L—_____ 、.、 11CFigure 11 105052-970519-fig.doc I --------1300006 Bu Yan C7K Jin Qing more) is replacing 100 L______, ., 11C oa 105052-970519-fig.doc 1300006Oa 105052-970519-fig.doc 1300006 105052-970519-fig.doc -9- 1300006105052-970519-fig.doc -9- 1300006 • 圖18 61 61b• Figure 18 61 61b •10- 105052-970519-fig.doc 1300006 θ年（月 &lt;曰修(更)正替換頁• 10-105052-970519-fig.doc 1300006 θYear (Month&lt;曰修(more) is replacing page 圖22 105052-970519-fig.doc -11 - 1300006 分年r月'兩修(更)正替換頁Figure 22 105052-970519-fig.doc -11 - 1300006 Yearly r month 'two repairs (more) positive replacement page 6565 圖23 66CFigure 23 66C 圖24Figure 24 圖25 105052-970519-fig.doc -12-Figure 25 105052-970519-fig.doc -12-
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